CN1070587A - Filtering system for muddy gas - Google Patents

Filtering system for muddy gas Download PDF

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Publication number
CN1070587A
CN1070587A CN 92103597 CN92103597A CN1070587A CN 1070587 A CN1070587 A CN 1070587A CN 92103597 CN92103597 CN 92103597 CN 92103597 A CN92103597 A CN 92103597A CN 1070587 A CN1070587 A CN 1070587A
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China
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pipe
tube
water
gas
filter
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CN 92103597
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Chinese (zh)
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麦松泉
麦恭铭
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麦松泉
麦恭铭
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Priority to CN 92103597 priority Critical patent/CN1070587A/en
Publication of CN1070587A publication Critical patent/CN1070587A/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D50/00Combinations of devices for separating particles from gases or vapours
    • B01D50/004Combinations of devices relating to groups B01D45/00 and B01D47/00
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D47/00Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/12Washers with plural different washing sections

Abstract

一种污浊气体过滤系统,包括烟尘过滤装置、滤袋过滤装置以及水液处理装置。 One kind of dirty gas filtration system comprising a soot filter means, processing means, and liquid water bag filter apparatus. 烟尘过滤装置中设有一烟尘流动管道及装设于该管道中的若干种强力喷雾器组,滤袋过滤装置中设有滤袋及污水输送管路,水液处理装置中设有复数的处理槽,用以对离开滤袋的水液作再处理与于利用。 Soot filtration device is provided with a dust flow duct mounted in the duct and the nebulizer several powerful groups, bag filter apparatus is provided with the filter bag and sewage transport conduit aqueous liquid processing apparatus is provided with a plurality of the processing tank, for liquid water leaving the filter bag for use in further processing. 本过滤系统中设有粒状烟尘收集装置,以将烟尘浓度极高的厂气中的颗粒较大的烟尘先行收集,再送入烟尘过滤装置进一步处理。 The filter system is provided with a particulate dust collecting means for further processing, to a larger high soot concentration in the gas plant dust particles collected in advance, and then fed to the soot filter means. 本过滤系统对于含有碳尘成分,油性成分,有恶味及有毒成分的废气,甚至于含高浓度灰尘微粒的污浊空气均能加以过滤处理。 This filtration system for carbon dust containing component, an oily component, evil smell and toxic exhaust gas components, even with high concentrations of dust particles in the air can be polluted filtering process.

Description

本发明为有关过滤废气或污浊空气的处理过滤系统,更具体地说,为有关将废气或污浊空气施以强力水雾喷洗,而过滤其中的烟尘,且处理下流的污水的系统与所设的装置。 The present invention is related to an exhaust gas filter or filter dirty air handling systems and, more particularly, is related to the exhaust gas or subjected to strong dirty air spray mist, wherein the soot filter, and the downstream sewage treatment system and established installation.

目前用以过滤污浊气体的方式及装置极多,产生的过滤效果亦各有不同,于诸方式当中,水洗法所应用的装置属较简单且较实用。 At present embodiment and the means for filtering dirty gas very much, resulting also have different filter effects, which Yuzhu embodiment, the case of water washing apparatus applied simpler and more practical. 下面将介绍几种现有的湿法处理装置。 The following describes several existing wet processing apparatus.

目前,对电力、石油炼制、钢铁厂等排出的气体基本上要进行脱硫处理,其主要流程及设备是利用鼓风机送出燃烧气体,经过冷却塔的冷却,再送入吸收塔,由吸收塔底部送入并冷却后排出气体,排出后的气体被上部来的稀硫酸将SO2气体吸收除去排入大气,而吸收SO2气体的稀硫酸则由吸收塔底部用泵泵送到氧化塔底部,并在催化剂作用下与送入塔底的空气中的氧气进气氧化生成硫酸。 Currently, gas discharged electricity, petroleum refining, steel mills and other substantially to desulfurization treatment, the main processes and equipment using the combustion gas feed blower, the cooled cooling tower, then into the absorption column, from the bottom of the absorber feed into the exhaust gas and cooled gas is discharged to the upper portion of the dilute sulfuric acid to remove SO2 gas absorption into the atmosphere, while the dilute sulfuric acid by absorbing SO2 gas absorption column to the bottom of the column by pump base oxide, and the catalyst oxidation with oxygen of the intake air into the bottom of the sulfuric acid generated in the action. 参见化工生产流程图解上册第440页,化学工业出版社。 See page 440 on volume of chemical production process diagrams, Chemical Industry Press.

而用于除去废气中的粉尘、烟气、雾汽的设备一般为干式或温式除尘器两种,其使用的装置有洗涤塔和电除尘器。 While the exhaust gas for removing dust, smoke, mist devices are generally a dry precipitator or two kinds of temperature, which means are used scrubbers and electrostatic precipitators. 参见化工生产流程图解443页,化学工业出版社。 See chemical production process diagram 443, Chemical Industry Press.

还有一种适用于除去恶臭成份和有害气体的斯特莱拉式脱臭装置,其基本结构是气体由塔的下部流入口送入,由于鼓风机的压力,使气体通过多孔板毛细管的细孔在各隔段上进行吸收之后,从塔的上部的除雾汽除去臭气并排出塔外。 There is also a Manchester type deodorization apparatus for removing Laila odor and harmful gas components applicable, its basic structure is fed from the lower portion of the gas inlet of the column, the pressure of the blower, the gas passes through the porous plate in the capillary pores after absorption of the upper compartment, an upper portion of the vapor from the demister column to remove the odor and is discharged outside the tower. 而供给多孔板的吸收液则依靠重力作用回到下部的循环槽内。 The absorbing liquid is supplied to the perforated plate by gravity action back to the lower portion of the circulation vessel. 另一方面,供给在毛细管上面的吸收液不下落,在毛细管表面上水平流动,经过回流管回到循环槽内。 On the other hand, the supply is not falling absorbing liquid in the capillary above the level on the surface of the capillary flow through the return conduit back to the circulation vessel. 参见化工生产流程图解上册第445页,化学工业出版社。 445 See album on chemical production process diagrams, Chemical Industry Press.

复合肥料生产中废气净化处理装置可参见苏联库兹涅佐夫著的化工厂大气污染防治一书的167页~169页,化学工业出版社。 Pages 167 - 169 production of compound fertilizer gas purification apparatus can be found in Soviet Kuznetsov significant air pollution control chemical book, Chemical Industry Press. 其基本原理是利用抽气机将废气抽至吸收塔进行冷却和湿润,然后送入率流式洗涤器中进行氟化物的捕集,率流式洗涤器是垂直安装的文丘里管,气体和喷淋碱液均由顶部进入洗涤器,由于流速大使气液强烈混合,使废气中的氟化物等组分被迅速吸收。 The basic principle is to use the exhaust gas aspirator pumped to the absorption column is cooled and humidified, and then into the flow rate for the scrubber fluoride trap, flow rate of the venturi scrubber is vertically mounted tube, and a gas by spraying lye into the top of the scrubber, since the flow rate of the gas-liquid mixed intensively ambassador, the fluorides in the exhaust gas components are absorbed rapidly. 然后气流混合物再进入分离器进行气液分离,分离后液体用离心泵重新打入率流式洗涤器喷淋吸收。 The mixture was then re-enter the gas stream separator for gas-liquid separation after re-separation of the liquid into a centrifugal pump with flow rate of the spray absorber scrubber. 然后,废气进入第二吸收塔进行脱酸等处理,最后经分离器,抽气机排出放空。 Then, the exhaust gas into the second absorption tower deacidification process and the like, and finally is discharged through vent separator aspirator.

从以上的废气处理系统可以看出,它们使用功能比较单一,即一种系统只能处理一种或相近的废气,而且其结构比较复杂,并均配置有适应性窄的分离器收装置。 As can be seen from the above exhaust gas treatment system, they use a single function, i.e., a system similar to handle only one or the exhaust gas, and its structure is complicated, and is configured with a narrow separator adaptive receiving device.

第二,它们所采中的吸收塔均为直式通道型的,而采用的均为水平喷淋系统,其废气迂回路线较短,经过时间短,过滤效果及灰尘杂质回落效果差。 Second, they are collected in the absorption tower straight passage type, and are used in the horizontal spray system, which exhaust detour shorter elapsed time is short, and the effect of dust and impurities by filtration down poor.

第三,各废气处理装置只能各自独立使用,无相配套的水处理及袋滤装置,故使用范围窄小,处理效果较差。 Third, each of the exhaust gas treatment apparatus can independently be used without supporting the bag and the water treatment means, so the use of a narrow range, the treatment effect is poor.

本发明的目的就在于克服现有技术所存在的上述缺点和不足,而提供一种由迂回烟尘过滤装置、滤袋过滤装置、水液处理及烟尘收集装置有机组构而成的污浊气体过滤系统。 The present invention overcomes the prior art is that the presence of the above-described drawbacks and disadvantages, and to provide a particulate filter by the bypass means, bag filters, water and liquid processing means has dust collection unit foul gas filtration system configuration formed by .

本发明目之一是为提供不同型式的具有流动管道与配置适当的强力喷雾器的烟尘过滤装置,使得污浊气体中的烟尘能适时地除去; One purpose of the present invention is to provide different types of smoke flow duct having a suitable strength and configuration of the nebulizer filter means, such that dirty gas in timely remove smoke;

本发明另一目的是为提供滤滤袋式的污水过滤装置,令自烟尘过滤装置中流下的污水,能有效地被过滤; Another object of the invention to provide a bag filter type sewage filter means, so that dust from the effluent stream in a filter apparatus, the filter can be efficiently;

本发明的另一目的是为提供水处理装置,以便经滤袋过滤装置的水液,作进一步的再处理、再回收而选回烟尘过滤装置中。 Another object of the present invention is to provide a water treatment device, so that the liquid bag through the water filtration device, for further reprocessing, and recycling the soot filter device selected from back.

本发明的另一目的是为提供浓烟尘收集装置,令颗粒烟尘成份极高的污浊气体,进入烟尘过滤装置的前,先经本浓尘收集装置、使得污浊气体中颗粒气体中的颗粒烟尘被收集于本浓烟尘收集装置。 Another object of the present invention is to provide concentrated dust collecting apparatus, so that high soot particle component dirty gas, before entering the dust filter means, concentrated first by the present dust collecting means, so that dust particles in the polluted gas particles in the gas is this concentration of dust collected in the collecting device.

本发明基本上亦系以水洗的技术,以达成污浊气体过滤的目的。 Also the present invention is substantially water-based technology in order to achieve the object dirty gas filtration. 不过为了强化污浊废气或污浊空气中的烟尘或灰尘的过滤效果,烟尘过滤装置在构造上采用形状特殊的迂回或旋转式的污浊气体流通管道,并配合强力喷雾器喷水雾的方向作适当配置,令水雾与污浊气体作充分混合,当污浊气体中烟尘或类尘与强力水雾混合后,其所流下的污水,则以滤袋过滤装置将的过滤,再经水处理设备的净化,回收再利用至烟尘过滤装置中的喷雾器上,高烟尘的污浊气体则先经过浓尘收集装置收集处理后再进入烟尘过滤装置,供应喷雾器的水液可依污浊气体中的烟尘成份不同而有改变;例如烟尘属性成份,供应这水液可为含有如肥皂、清洁剂的去油剂者,烟尘属有恶味或有毒性成份,供应的水液可为含有石灰、冷冻水者,使得到致较佳的过滤效果。 However, in order to strengthen the effect of filtering dirty exhaust foul air or smoke, or dust, soot filter means takes the form of a special bypass or rotary dirty gas flow in the conduit structure, and with the strong direction of spraying with water fog properly arranged, so as mist and foul sufficiently mixed gas, when the water mist mixed polluted gas with soot or dust strength class, they shed the water, places the bag filter filtration apparatus, and then by the water purification equipment, the recovery on the particulate filter to recycle the nebulizer apparatus, dirty gas having a high dust collecting means collects the first processing unit through the filter before entering the soot dust concentrated, aqueous liquid supply atomizer to follow smoke components differ dirty gas is changed; e.g. smoke component properties, this water supply may contain as liquid soaps, detergents degreasers who smoke or toxic metal evil smell components, liquid may be supplied water containing lime, by chilled water, so to obtain a more electroluminescent excellent filtering effect. 本过滤系统中所揭露的烟尘过滤装置,有许多不同的型式,可令使用者依其所需,作适当的选择。 The filter system disclosed soot filter device, there are many different types, may be required to make the user to easily make appropriate choices. 尚且,在烟尘过滤装置中,有一种型式系针对炼油厂的燃烧塔所排放的废气而设,亦有可设置于大型轮船上用以过滤轮船排放的废气者。 Yet, the dust filter device, there is a type of system for the emissions of combustion refinery tower and provided, also may be provided on large ships to filter the ship's exhaust emissions. 因此,本过滤系统所能适用的范围极广,深具实用性。 Thus, the present filtration system can apply a very wide range, deep practicality.

由上可见,本发明的显著效果是:第一,将烟尘过滤装置、滤袋过滤装置、水处理设备及烟尘收集装置按最佳处理流程最佳地有机结合起来,使废污气体的净化处理得以在一个系统内完成。 Seen from the above, a significant effect of the present invention are: first, the dust filter device, the filter bag apparatus, dust collection equipment and water treatment equipment in accordance with optimal processing flow optimally combine the purification of waste gas polluted It is completed within a system.

第二,烟尘过滤装置采用的是曲折迂回的或螺旋绕盘式的管道,加上在管道不同的方位设置有强力喷雾器组,故使烟尘所经过的除尘路线加长,而浸湿降尘效果增加。 Second, dust filter means uses a meandering or spiral wound pipe disk, coupled with a strong atomizer provided in different sets of pipes orientations, so that the soot dust route passes lengthened, the effect of increasing the wet dust.

第三,水处理装置既可将滤袋过滤装置流下来的污水进行处理净化,而且可使其循环利用,即用于烟尘收集装置的冷却使用。 Third, the water treatment device can bag filter apparatus flows down sewage purification processes, and it can be recycled, i.e. for cooling the dust collecting device used.

第四,该系统可依次串接使用,也可按实际需要选择其中的某些设备使用,因而,具有较大的灵活性和适应性。 Fourth, the system may be used sequentially connected, also according to the actual need to select certain devices used therein, and therefore, have greater flexibility and adaptability.

第五,该系统可视处理对象的不同而采用不同的喷雾介质,以满足对不同组份的烟尘、恶臭气体的处理需要。 Fifth, the system is different from the visual processing target using different spray medium, to meet the different compositions of the fumes, the process needs to malodorous gases.

本发明的具体结构是由下面的实施例及其附图实现的:图1为本发明的污浊气体过滤系统中的迂回型烟气过滤装置的一实施例的剖视示意图。 Specific structure of the present invention is composed of the following examples and the accompanying drawings implemented: a schematic cross-sectional view of the embodiment of FIG. 1 dirty gas filtration system of the present invention the bypass flue gas type filtration apparatus.

图2为图1烟尘过滤装置中废气入口处的冷却管段的详细剖视示意图。 Figure 2 details a schematic cross-sectional view of a cooling tube apparatus at the inlet section of the exhaust gas is soot filter 1 of FIG.

图3为图2中沿AA线的剖视示意图;用以表示冷却水流动空间及冷却进水管与出水管之间的关系位置。 3 is along a line AA in FIG. 2 is a schematic cross-sectional view; to indicate the flow of cooling water into the cooling space and the relationship between the position and outlet pipe.

图4为图2及图3中冷却进水管的立体示意图。 FIG 2 and FIG 4 is a diagram of the cooling water inlet pipe 3 is a schematic perspective view.

图5为图1中烟尘过滤装置中迂回管道的各管段的端部连接一例的立体示意图。 FIG 5 is a perspective schematic view of an end portion of FIG tube sections in the bypass conduit means connecting an example of a soot filter.

图6是图1中强力喷雾器组为长板形的复数组设置形式。 FIG 6 is a view in a powerful set of complex nebulizer group provided in the form of a long plate shape.

图7是图1中强力喷雾器组为单管形的多喷头结构形式。 FIG 7 is a multi-nozzle structure in FIG. 1 as a single set of sprayers strength tubular.

图8是图1中强力喷雾器组为单管形的多喷头的另一种结构形式。 FIG 8 is a powerful set of nebulizer to another as a single structure plurality of tubular nozzle.

图9是图1中强力喷雾器组为圆板形的结构形式。 9 is a strong structure in FIG. 1 atomizer disk-shaped group.

图10是图1中强力喷雾器组为圆板形的另一种结构形式。 FIG 10 is another strong structure in FIG. 1 atomizer disk-shaped group.

图11是图1中强力喷雾器组为圆板形的第三种结构形式。 FIG 11 is a third strong structure in FIG. 1 atomizer disk-shaped group.

图12是图1中强力喷雾器组为圆板形的第四种结构形式。 FIG 12 is a fourth configuration in FIG. 1 in the form of a circular plate set nebulizer strong shape.

图13为本发明污浊气体过滤系统中迂回型烟尘过滤装置的另一实施例的剖视示意图。 Dirty gas filtration system lead-type dust cross-sectional view of another embodiment of a filter apparatus 13 of the present invention, FIG.

图14为与图13烟尘过滤装置相似的又一实施例,极合适大型轮船上使用。 FIG 14 is similar to the embodiment of the particulate filter 13 means a further, very suitable to use on large ships.

图15为本发明污浊气体过滤系统中迂回型烟尘过滤装置又另一实施例,极适合排放高尘废气的过滤。 15 dirty gas filtration system lead-type dust filter means yet another embodiment of the present invention very suitable for high filtration dust exhaust emissions.

图16为本发明污浊气体过滤系统中直型烟尘过滤装置的一实施例。 FIG dirty gas filtration system 16 straight soot filter device according to an embodiment of the present invention.

图17为本发明污浊气体过滤系统中,应用于过滤炼油厂燃烧塔废气的烟尘过滤装置实施例的立体示意图。 FIG dirty gas filtration system 17 of the present invention, the filter applied to refinery tower combustion exhaust soot filter means perspective schematic of an embodiment.

图18为图17烟尘过滤装置中第一阶段过滤部分剖视示意图。 FIG 18 a schematic cross-sectional view of part of the first stage filter means is a filter 17 soot FIG.

图19为图17烟尘过滤装置中第二阶段过滤部分剖视示意图。 FIG 19 a schematic cross-sectional view of the second stage of the filter means is a filter section 17 in FIG soot.

图20为图17中烟尘过滤装置应用于具有三个燃烧塔排气口并列时,其第一阶段过滤部分平面剖视示意图。 FIG 17 FIG 20 is applied to the soot filter device having three parallel combustion vent column, a first filter stage partial plan sectional view.

图21为本发明的污浊气体过滤系统中,应用于过滤污浊空气的烟尘过滤装置实施例的剖视示意图。 Dirty gas filter system of the present invention in FIG. 21, the dirty air is applied to the filter cross-sectional view of the dust embodiment of the filter apparatus.

图22为图21中吸尘装置与网件固定方式的示意图。 21 is a schematic diagram of FIG. 22 and the dust collecting attachment member fixed network mode.

图23为图21中沿AA线的剖视示意图,表示吸尘装置的前视形状。 FIG 23 FIG 21 is a cross-sectional view along line AA schematic front view showing the shape of the suction device.

图24为图21中沿BB线的剖视示意图,表示网件的前视图。 24 is along the line BB in FIG. 21 a schematic cross-sectional view, a front view of a web member.

图25为图21图中挡水器的A向示意图。 FIG 25 FIG 21 FIG retaining an A to FIG.

图26为图25中挡水器的俯视示意图。 FIG 26 is a schematic top view of a mist eliminator 25.

图27为图21中输气管道后段部分侧视示意图,表示挡水器固定于输气管道上的部位。 FIG 27 is a partial side view of the rear section of the gas pipeline 21, showing the retaining portion is fixed to the pipeline track.

图28为图25中挡水刷组合形成多列的示意图。 FIG 28 FIG 25 is a schematic view of a combination brush retaining a plurality of columns formed.

图29为图21中前端口网盖的B向示意图。 FIG 29 is a front net lid port B of FIG. 21 to FIG.

图30为图21中输气管道设置喷雾器部位CC剖面剖视示意图。 FIG 30 is a sectional view CC portion is provided in the nebulizer gas pipeline sectional view in FIG. 21.

图31为粒状烟尘收集器的前视示意图。 FIG 31 is a particulate soot collector front view.

图32为图31中粒状烟尘收集器的右侧视示意图。 FIG 32 is a right side in a particulate soot trap of a schematic view of FIG. 31.

图33为图31中粒状涸尘收集器的左侧视示意图。 FIG 33 is a left side view showing the particulate dry dust collector 31 of FIG.

图34为图31中粒状烟尘收集器的收集筒的剖视示意图。 FIG 34 FIG 31 is a cross-sectional view of the particulate dust collection tube collector.

图35为图34中沿AA线的剖视示意图。 FIG 35 FIG. 34 is a sectional view along line AA in FIG.

图36为图34中沿BB线的剖视示意图。 FIG 36 FIG 34 along the line BB cross-sectional view of FIG.

图37为图31中粒状烟尘收集器中的收集袋内部构造。 FIG 37 is an internal structure of the particulate collection bag dust collector 31 of FIG.

图38为本发明污浊气体过滤系统中,滤袋过滤装置实施例的立体示意图。 FIG dirty gas filtration system 38 of the present invention, the bag filter means perspective schematic of an embodiment.

图39为本发明污浊气体过滤系统中,水液处理装置的一实施例剖视示意图。 FIG dirty gas filtration system 39 of the present invention, one case of a schematic cross-sectional view of the liquid processing apparatus of the embodiment of the water.

图40为本发明污浊气体过滤系统中,水液处理装置的另一实施例的俯视示意图。 Dirty gas filtration system, a schematic plan view of another embodiment of the aqueous liquid processing apparatus of the embodiment 40 of the present invention FIG.

图41为图40中水液处理装置的A向部分剖视示意图,表示搅拌槽与清水槽的管路配置情形。 FIG 40 FIG 41 is a water A liquid processing apparatus according to a schematic cross-sectional view partially showing the case of plumbing configuration stirred tank and clean water tank.

图42为简便式滤袋过滤及水液处理组合装置实施例的剖视示意图。 Figure 42 a schematic cross-sectional view and filtered aqueous treatment composition embodiment of apparatus according to the simple formula for the bag.

图43为图42中简便式滤袋过滤及水液处理组合装置的外观立体示意图。 FIG 43 is a bag filter 42 and the appearance of a simple formula aqueous treatment composition schematic perspective apparatus.

下面将结合附图1~43对本发明的具体结构进行详细地说明:本污浊气体过滤系统由迂回式烟尘过滤装置2、滤袋过滤装置8、水液处理装置101,烟尘收集装置3组构而成,烟尘过滤装置本身是一迂回或螺旋盘绕式管道2,在管道2内设置有若干强力喷雾器组6,经烟尘过滤装置过滤后流下的污水经其自身底部设置的污水下流管道25流出并进入到滤袋过滤装置81中过滤,然后流入具有复数个串连沉淀槽1014的水处理装置101中进行净化处理后再返流至烟尘过滤装置内的各强力喷雾器组6循环使用,经烟尘过滤装置2过滤后的新鲜烟气经其自身上部的烟气排出通道21排出,污浊气体是由烟尘过滤装置2底部的废气管1直接进入到迂回或螺旋盘绕式管道2中进行直接过滤或先进入烟尘收集装置3后、再进入到烟尘过滤装置2中进行过滤的,在烟尘过滤装置2内设置有强力送风机4。 1 following with reference to 43 the specific structure of the present invention will be described in detail: The dirty gas filtration system apparatus to a bypass dust Formula 2, bag filter means 8, the liquid processing apparatus 101 water, dust collecting means and the fabric 3 into the soot filter apparatus itself is a circuitous or spiral wound conduit 2 disposed in the conduit 2 has several strong nebulizer group 6, the soot filter apparatus after the stream of water flowing out and into through the sewage downflow conduit of its own provided in the bottom 25 bag filter to filter device 81, and then flows into the purification treatment having a plurality of water treatment apparatus 101 series precipitation tank 1014 and then to reflux soot filter within each group nebulizer strong recycling device 6, by the soot filter means fresh flue gas exhaust pipe 2 through which the filtered exhaust passage 21 of the upper portion of the flue gas itself discharged by the dirty gas soot filter device 1 of the base 2 or directly into the bypass conduit in a spiral wound filter 2 or directly into the first smoke after collecting device 3, and then proceeds to the soot filter filtering device 2, the soot filter is provided in the apparatus 2 has a powerful blower 4. 参见图1、图13至图17及图31、图37和图39。 Referring to Figure 1, 13 to 17 and 31, 37 and 39.

本发明中迂回烟尘过滤装置2的结构特点是:它是迂回型烟尘过滤装置之一种结构形式,它主要由一形如S形的迂回管道2,一复数的强力喷雾器601、602、603,一强力送风机4,一过滤件22等构件组成。 In the present invention bypass the structural characteristics of the soot filter device 2 is: It is a lead-type structure of the soot filter apparatus, which is mainly composed of a shape such as S-shaped bypass pipe 2, a plurality of sprayers 601, strong, 4 a strong blower, a filter element 22 composed of other components. 该迂回管道2中的各管段的端部,均有一连接端接头23,由于迂回管道2最底部的管段废气进口处附近的进风端与最上部的管段的出气端口为无接头的装置,故利于废气的进入与轻新空气的离开。 Ends of the tube section 2 of the bypass duct, has a connection terminal tab 23, since the outlet port inlet end near the bypass duct pipe exhaust gas inlet 2 bottommost tube segment uppermost for device connection free, so in favor of leaving the exhaust gas into the air with a new light. 燃烧器或燃烧炉废气排出管1的出口端与本迂回管道2的最底部管段接合,以便废气能顺利进入本迂回管道2。 A combustion burner or furnace gas outlet end of the discharge pipe 1 with this bypass line 2 bottommost pipe section engages, so that the exhaust gas can successfully enter the bypass duct 2 of the present. 强力送风机4的主要功用为令进入迂回管道2的废气能沿着迂回管道2向上迂回前进,强力喷雾器601的主要功能为刚进入迂因管道2的热废气一方面冷却,一方面与废气充分混合,以便废气中烟尘与水雾结合。 The main function of a strong blower 4 is to make the exhaust gas into the bypass conduit 2 can be snaked 2 upwardly along the bypass conduit, the main function of nebulizer 601 is strong just entering the circuitous exhaust conduit 2 by heat aspect cooled, mixed with the exhaust gas on the one hand for binding dust in the exhaust gas with an aqueous spray. 直立式强力喷雾器组602分别装设于各管段接头23处与空气出口端处的直立管段,除了设于空气出口端处的强力喷雾器602外,其他强力喷雾器组602中喷头方向均令强力水雾沿着废气流动方向推送,用以一方面前推废气流动,一方面与废气作充分混合,横置的强力喷雾器组603则设于各管段的顶部,装设诸强力喷雾器组603的目的是为配合诸强力喷雾器组602,令迂回往上流动的烟气能与水雾达到真正混合,同时为顾及水雾与烟尘混合后的污水,能往下流动至出口管25,整个迂回管道2的下半部管段所装设的强力喷雾器组603中的喷头方向配置成令强力水雾沿着废气流动方向推送,而上半部管段的强力喷雾器组603中的喷头方向则配置成令强力水雾往相反于废气流动方向推送,尚且设于迂回管道2末端的清新烟气出口端21处的直立喷雾器组602的喷头方向亦配置成令强 Upright strong nebulizer group 602 are respectively mounted to the respective tubular section joints 23 end the air outlet of the upright pipe section, in addition to strong atomizer 602 disposed in an air outlet end, other powerful nebulizer group 602 in the head direction are so strong mist pushed along the exhaust gas flow direction, the exhaust gas flow prior to pushing the one hand, on the one hand adequately mixing with the exhaust gas, a strong transverse nebulizer group 603 is provided on the top of each tube section, the purpose of such strong mounted sprayer 603 is set with such strong nebulizer group 602, so that the flue gas flowing upward detour can achieve true mixed with water mist, as well as taking into account the water mist mixed with dust, can flow down to the outlet tube 25, the whole of the bypass duct 2 half portion of the head pipe installed powerful nebulizer group 603 is configured to make a strong push mist along the exhaust gas flow direction, and the direction of the nozzle group 603 sprayers strong upper half tube section is arranged in order to strong mist an exhaust gas flow direction opposite to the push, yet provided in the bypass pipe end 2 fresh flue gas outlet end 21 of the upright direction of the sprayer nozzle set 602 also arranged so strong 水雾往相反于烟气流动方向喷送。 Mist in the flue gas flow in the opposite direction of blowing. 有一滤水刷件22位于该出口端21中,当过滤后的烟气通过该刷件22后可令其中所含的水分不随烟气离开。 A brush member 22 has drainage located at the outlet end 21, when the flue gas is filtered by the brush member 22 so that the moisture contained therein can not leave with the flue gas. 迂回管道2的长短可依燃烧炉通常排出的废气所含烟尘浓度而定,即若废气中烟尘浓度高,可装设较长迂回管道2,烟尘浓度低则可设置较短迂回管道2。 Bypass conduit 2 may vary depending on the length of the combustion furnace may be generally contained in an exhaust gas discharged from the dust concentration, i.e., when the high dust concentration in the exhaust gas, the pipe 2 can be equipped with bypass long, low dust concentration can be set shorter bypass duct 2. 再者,强力喷雾器组602、603所使用液体,亦可依烟尘成分差异而使用一般纯水、冷冻水、肥皂水、石灰水,或其他适当的清洁液。 Furthermore, a strong liquid used nebulizer group 602, may also be used according to differences in smoke constituents generally water, chilled water, soapy water, lime, or other suitable cleaning fluid.

其次,请参见图2、图3及图4,其中图2所示为迂回管道2在烟气入口处部分以螺栓固定方式可分离的短管段24。 Secondly, see Figure 2, 3 and 4, shown therein is a bypass conduit 2 2 at the inlet portion of the flue gas in a fixed manner bolt detachable short pipe section 24 in FIG. 由于离开燃烧炉排气管1烟气系属高温烟气,因此迂回管道2在烟气入口处部分所使用的材料为耐高温者,为了降低材料受热后的高温度,该部分可设成短管段24,且环绕该管段24大部分周围有一容纳冷却水的空间244,冷却水由冷却水进管241进入该空间244,并借由冷却水出管245离开短管段24。 Since the high temperature flue gas leaving the combustion grate system genus flue pipe 1, so the material in the flue gas bypass conduit 2 at the inlet portion is a high temperature are used, in order to reduce the high temperature of the heated material, the portion may be set to be shorter tube section 24, and surrounds most of the periphery of the tubular section 24 having a receiving space 244 of the cooling water, the cooling water from the cooling water intake pipe 241 into the space 244, and by means of a cooling water pipe 245 a short pipe section 24 away. 图3与图4所示为冷却水进管241位于空间244中的位置及形状。 As shown in FIG. 3 and FIG. 4 is a cooling water intake pipe 241 is located in the position and shape of the space 244. 冷却水进管241有一圆弧形管部,且于该圆弧形管部两下端,分别水平延伸一略短于短管段24长度的水平管部242,而各该水平管部242的底面有一复数的小出水口243,以便将冷却水送入短管段24的冷却水容纳空间244中。 Cooling water intake pipe 241 has a circular arc-shaped tube section, and at two lower end of the arc tube portion, each extending horizontally a little shorter than the 24 length of the short tube section horizontal pipe part 242, the bottom surface of each of the horizontal tubular portion 242 has a a plurality of small outlet 243, so that the cooling water into the cooling water receiving space 24 of the short tube segment 244. 冷却水进管241与冷却水出管245均固定于短管段24处,冷却水循环可以自然的重量式循环流动或以泵压的机械式循环流动方式。 Cooling water intake pipe 241 and the coolant outlet pipe 245 are fixed to the short pipe section 24, a cooling water circulating naturally circulating gravimetric or mechanical pump cycle flow pattern.

图5为迂回管道2各管段端以接头23连接之一例子,该接头23形如长方形箱子配以两凸缘形管接头,而各管段为圆管,与接头23固定一起部分呈凸缘形,以便以螺栓与防漏垫片与接头23螺固。 FIG 5 is a pipe section 2 of each end of the bypass pipe joint 23 is connected to one example, the connector 23 shaped like a rectangular box-shaped connector coupled with two flanges, the tube sections of pipe, the joint 23 is fixed with a flange-shaped portion , so as to be leak-proof gasket and the joint bolt 23 is screwed. 迂回管道2各管段断面并非一定要圆管,方形管或长方形管,其他适当的管断面形状也可适用。 Each pipe section 2 pipe does not have to bypass tube, square tube or a rectangular tube, other suitable tubular cross-sectional shape is also applicable. 总的,各管段的断面形状,可依实用场合需要而定,并非限定为圆管形。 Overall, cross-sectional shape of each pipe section, as occasion demands may be useful to follow, it is not limited to a circular tube.

图6~12所示为强力喷雾器组602、603可适用的形式,第6图的强力喷雾器组602、603为长板形,喷雾器组周围的凸缘231及螺栓孔,是为了配合防漏垫片螺固至迂回管道端接头23与各管段上,但各管段需为方形断面或长方形断面,或装设强力喷雾器组处为平面使其可应用板形喷雾器。 As shown in FIG. 6 to 12 in the form of a nebulizer strong applicable group 602, 603, 602, 603, the group of strong nebulizer FIG 6 is a long plate shape, set around the flange 231 and the bolt holes nebulizer, with leak-proof pad to sheet is screwed to the bypass conduit end fitting 23 on the respective tube sections, but it must be a rectangular tube sections or rectangular cross-section section, strong nebulizer or fitted so as to be set at a flat plate-shaped nebulizer application. 图7与图8的强力喷雾器组602、603系属单管形,图8所示的喷雾器组上的喷头系平均配置于管件60上的不同方向,以加强喷雾效果。 Strong group 602 based nebulizer 7 and FIG. 8 is a single tubular, nebulizer nozzle group based on the average arrangement shown in FIG. 8 in different directions on the member 60, to enhance spray effect. 图9与图10所示的强力喷雾组602、603为圆板形,两者的式样大同小异,图9喷雾器组的水系由中央流至周围,而图10喷雾器组则由侧边往各处流动。 9 and FIG strong spray group 10 shown in FIG. 602 is a circular plate shape, similar patterns of both, the aqueous stream 9 to FIG sprayer set around the central group of the sprayer 10 to the entire flow side by FIG. . 两者的周缘附近均设有等距之一复数螺栓孔,以便能配以防漏垫片而螺固至迂回管道2上。 Both of which are near the peripheral edge is provided with one of a plurality of equally spaced bolt holes so as to together with leak-proof gasket to be screwed on the bypass line 2. 图11与12所示为另一种圆板形喷雾器组,即加装有送风机62,可加强水雾推送及烟气推送效果,极为合适设于接头23处。 FIG 11 is a circular plate-shaped nebulizer another group, i.e., there is installed the blower 62 in FIG. 12, can enhance the effect of pushing the flue gas and mist push extremely suitable provided at a joint 23. 如图6所示的长板形喷雾器组也可制成弧板形,以利装设于迂回管道2中的各管段为圆管壁或圆弧管壁上。 FIG elongated plate 6 shown nebulizer group can also be made arc-shaped plate, to facilitate bypass duct 2 is mounted on each pipe section wall on a circle or arc tube wall.

图13为本发明迂回过滤装置的另一种型式。 FIG 13 detour another type filtration apparatus of the present invention. 管道2为圆筒形,其中有一螺旋导板3,该螺旋导板3的周围为固定于管道2的内壁上。 Conduit 2 has a cylindrical shape, which has a helical guide plate 3, around the helical guide plate 3 is fixed to the inner wall of the pipe 2. 螺旋导板3中央部位有一水液下流中管31,该中管31与螺旋导板3接触部分,设有复数孔洞32,以令螺旋导板3上部的污水亦可经由该复数孔洞32进入该中管31下流。 3 the central portion of the spiral guide plate has a liquid water downflow pipe 31, the third contact portion of the pipe 31 and the spiral guide plate provided with a plurality of holes 32, in order to make the spiral guide plate 3 the upper part of the sewage can 32 enters the pipe 31 via the plurality of holes dirty. 藉由强力喷雾器6适当配置,使得由燃烧炉排管1来的废气接受强力送风机4与强力喷雾器61的推送,在管道2内沿着螺旋叶板3所围成的螺旋空间上移,废气中烟尘与水雾混合后亦沿着螺旋导板3下流,或由中管31各孔洞32下流,下流污水由管道2底部的排出管25离开,并进入滤袋过滤装置(见图16)。 6 by a suitably configured nebulizer strong, so that the combustion exhaust gas of the grate tubes receiving powerful blower 4 and the push strength of the sprayer 61, move along the helical space surrounded by the spiral vane 3 in the pipe 2, the exhaust gas after mixing with the smoke downstream mist also along the spiral guide plate 3, or the apertures 32 Central tube 31 downstream, the downstream exhaust pipe 2 from the water leaving the bottom of the duct 25, and into the bag filter means (see FIG. 16). 清新烟气则由管道2顶部L形排气管21离开,排气管21的末端设一防尘盖211,在本迂回管道装置未运转时,防止雨水或污尘进入管道2。 Fresh flue gas duct 2 by an L-shaped top 21 away from the exhaust pipe, the exhaust pipe 21 is provided a dust cover end 211, the bypass duct when the present apparatus is not in operation, to prevent rain water or dust and dirt into the pipe 2. 再者管道2下方适当处亦可设置一抽水泵5,与中管31以连接管51连通,以便将中管下流的水再送至螺旋导板3处,且水液被泵送的方向,亦为废气流动方向,协助强力喷雾器6冲洗效果。 Note that below the pipe 2 may also be provided at a suitable suction pump 5, the tube 31 is connected to the communication pipe 51, so that water flowing down the tube coil and then sent to the guide plate 3, and the direction of the water being pumped liquid, also an exhaust gas flow direction, to assist atomizer 6 strong washing effect. 由于本迂回管道装置系属大型烟气过滤装置,因此,管道2的靠近底部的侧边设一人孔22,以便维修人员进入管道2中行维护与修理工作。 Since this is a large bypass conduit means based smoke filter device, therefore, the pipe 2 near the bottom side of a manhole 22 is provided to maintenance personnel into the conduit 2 rows maintenance and repair work. 于废气排管1与管道2连接处的管道2管段,亦可设成如图2、图3与图4所示的冷却管装置配合结构,以降低该部分的管段温度。 In the exhaust gas discharge pipe 12 and the pipe segment at the pipe connection pipe 2 can also be set to 2, 3 and condenser mating structure of the apparatus shown in FIG. 4, in order to reduce the temperature of the portion of the pipe section.

图14是与图13类似的迂回过滤装置的一实施例,在管道2底部有一底板24令一复数废气排管1伸通吞近其一侧适处,而不同于图13中的仅是废气排管1的方式。 FIG 14 is an embodiment similar to the embodiment of FIG detour filter means 13 has a bottom plate 24 so that a plurality of gas discharging pipe extending through a side thereof adapted to swallow nearly at the bottom of the pipe 2, whereas in FIG. 13 differs only in the exhaust gas embodiment 1 of the drain pipe. 整个管道2成下宽上窄的倾斜造形,且管道2任何高度处的横断面形状略成椭圆形或圆形。 2 to the entire width of the narrow inclined pipe shape, and the cross-sectional shape of the conduit 2 at any height slightly oval or circular. 管道2近顶部为一向中央倾斜的顶板21,且该顶板21中央有一往下延伸一段距离的流通孔211,令清新烟气通过与令顶板21外的水、如雨水等能经该流通孔211下流至中管31。 Near the top of the pipe 2 is always the center of the top plate 21 is inclined, and the center of the top plate 21 has a flow bore 211 extends a distance downward, so that the flue gas by the fresh water make the outer top panel 21, such as rainwater can flow holes 211 through which to the downstream tube 31. 由于有强力送风机作用,令废气能持续往上迂回流动,不会因流通孔211直径较小,而令清新烟气无法上移。 Because of the strong role of the blower, so that the exhaust gas can continue to flow up the roundabout, not because of the smaller diameter flow hole 211, and the smoke can not make fresh move. 本迂回管道2极合适多废气排管的废气过滤,在实用场合上可应用在轮船烟囱,对轮船所排放的废气清理非常有效。 This bypass conduit 2 suitable multi-pole gas filter exhaust gas discharge pipe, in practical applications can be used in the chimney ship, the ship is very effective for cleaning the exhaust gas emissions.

图15所示为又一迂回过滤装置的另一实施例。 Figure 15 shows another further embodiment of the bypass filter means. 由本剖视图可看出管道2为形如锯齿形管路,管道2底部具有较宽大的空间,用以令高压废气排管1与普通的废气排管11伸通到底板24之一侧并而进入该较宽大的空间,底板24的另一侧则为污水排出管口25。 This can be seen from the sectional view of the pipe 2 is shaped like a zig-zag line, the base pipe 2 has a wide large space for the exhaust gas discharge tube 1 so that the high-pressure side and the common drain pipe 11 extending through the exhaust gas in the end plate 24 and into the the wider a large space, the other side of the bottom plate 24 of the discharge nozzle 25, compared with the sewage. 管道2的顶部呈水平形且固设一清新气体排出管21。 The top of the pipe 2 is fixed in a horizontal shape and a fresh gas discharge pipe 21. 诸强力喷雾器组601、602、603分别装设管道2中锯齿形各侧适的相间隔位置处,管道2顶部排出管2的旁边水平顶处也设有一强力喷雾器组成603。 At such a position spaced groups 601, 602 are mounted sprayer strength conduit 2 suitable zigzag each side of the top of the duct 2 at the top level next to the discharge tube 2 is also provided with a powerful composed 603 sprayer. 管道2邻近底板24之一侧倾斜侧设有大小适当的挡板23,该挡板23下端系固定于管道2的内壁,其上端则为自由端。 2 adjacent the side of the bottom plate 24 of the duct is provided with suitable size inclined side shutter 23, the shutter 23 is fixed to the lower end line of the pipe wall 2, its upper end was free. 一强力弹簧22设置于挡板23背部靠近上端处与管道2的内壁间,且该弹簧22的一端固定于挡板23的中央,弹簧22另一端则固定于管道2的内壁。 A strong spring 22 is disposed between the inner wall near the back of the baffle 23 at the upper end of the pipe 2, and one end of the spring 22 is fixed to the center of the other end of the spring plate 22 is fixed to the inner wall 23 of the pipe 2. 当高压力的废气上行时,将碰击挡板23,因碰击产生撞击力则由强力弹簧22所吸收,并使得挡板23前后摆动,高压废气也因此流速减缓,并沿着迂回管道2向上流动。 When the high-pressure exhaust gas line, the shutter 23 hitting, crashing due to impact force generated by the power spring 22 is absorbed, and swing back and forth so that the shutter 23, thus to slow down high pressure exhaust gas, and along the bypass conduit 2 flows upward. 由于强力喷雾器组601、602、603所喷出的水雾中含石灰、去污剂的成份,其与向上流动的高压废气作充分的混合,使高压废气中有味有毒成份的烟气因弥漫于强力水雾中,而与其合为污水并下流至底板24处的污水排管25而离开管道2。 Since strong nebulizer group 601,602,603 ​​containing the ejected mist of lime, detergent ingredients, with the high pressure exhaust gas flowing upwardly for sufficient mixing, the high-pressure exhaust gas due to odorous fumes diffuse toxic components mist in strength, and its combined sewage and wastewater flows down to the bottom plate 24 of the discharge tube 25 exits the duct 2. 普通非高压废气,经由废气排管11而进入管道2,在废气往上流动时,同样可以强力喷雾器组601、602、603所喷出的水雾将废气中烟尘过滤。 Common non-high pressure exhaust gas via the exhaust gas discharge pipe 11 into the pipe 2, when the exhaust gas flows upward, the group may also be a strong nebulizer 601,602,603 ​​mist ejected soot filter in the exhaust gas. 由于某些化学工厂需要作间断性排放高压液化煤气或氯化气,或其他高压的具臭味或有毒气体,使用本迂回管道废气过滤装置时,可配合排放压力,对强力喷雾器组喷水雾的时机,作适当的控制,使得高压气体排放时,强力喷雾器组能适时地喷出水雾,以与高压气体作充分混合,使得高压气体中的臭味、有毒成份、烟尘等能与水雾一起下流,而成为污水,以便作进一步的处理。 Since some chemical plants need to make a high pressure liquefied gas discharged intermittently or chlorinated gas, or with other odors or toxic gas pressure, the use of this exhaust gas filter bypass conduit means, can be used with discharge pressure, water mist sprayers group of strong when the timing is appropriately controlled, so that the high pressure gas discharge, strong nebulizer group timely ejected mist, to be mixed with the high pressure gas, so that the high pressure gas odor, toxic components, dust and the like can mist dirty with, and become water, for further processing. 对于借着排放压力控制强力喷雾器组的喷水雾时机,可以一般常用的压力控制开关控制,例如当高压气体达到泄放压力的85%时,压力控制开关可令第一段强力喷雾器组601开始喷水雾,当高压气体达到泄放压力90%时,压力控制开关可令第二段强力喷雾器组602开始喷水雾,当高压气体达到泄放压力的95%时,压力控制开关可令第三段强力喷雾器组603开始喷水雾,一旦高压气体达到泄放压力时,泄放阀便令高压气体喷出,使其与诸强力喷雾器组的水雾作充分的混合。 For the discharge pressure by controlling the timing of spraying water sprayer strong group, can generally be used to control a pressure control switch, for example, when high-pressure gas reaches the relief pressure of 85%, the pressure control may not render the first switch group 601 start strong nebulizer spraying water, when the high pressure vent gas reached 90%, the pressure control switch 602 so that the second segment group strongly nebulizer starts spraying water, high-pressure gas when the pressure reaches 95% of bleed, the pressure can make the first control switch strong group three sections 603 starts spraying water sprayer, once the high-pressure gas reaches a pressure relief, the relief valve has made the high-pressure gas discharge, and sufficiently mixed with the mist nebulizer group such as strength. 当高压气体泄放后,压力逐渐降至泄放压力的85%以下时,压力控制开关便令所有的强力喷雾器组停止喷水雾。 When the high-pressure gas venting, the pressure was gradually reduced to 85% of the relief pressure or less, then the pressure control switch is set so that all the stop water mist sprayers strength. 此种利用高压气体本身的压力作开关强力喷雾器组的方式,由于不需要操作人员接近,极具安全性。 Using a high-pressure gas such as the mode switch itself strong nebulizer group, since the operator does not need to close, highly safety. 此外,利用电子遥控器配合高压气体的压力,以进行强力喷雾器组开关控制也可达到相同效果。 In addition, the use of high pressure gas with an electronic remote control pressure to the switching control group for strong nebulizer can achieve the same effect.

图16所示为烟尘过滤装置的又一个实施例,其为横向直型式。 As shown in FIG. 16 is a soot filter device according to yet another embodiment, which is a straight lateral type. 由该图中可得知输气管2分成三段,它们分别为第一输气段201,第二输气段202及第三输气段203,为适应实际上的需要,也可减少或增加输气段的段数,除了进气端设有抽风扇51外,于各段均设一调节气流的风扇52、53及54,配合输气管2壁上所设置的复数喷雾器对废气作过滤,其流下的污水,依其污浊程度而使用适当的污水处理装置加以过滤。 This figure can be learned from the pipeline 2 is divided into three sections, respectively a first gas transmission section 201, a second gas delivery section 202 and a third gas delivery section 203, to meet the actual need, can be reduced or increased the number of stages of gas transmission section, in addition to the inlet end is provided with suction fan 51, the segments are located in a gas flow regulator 52, 53 and the fan 54, with a plurality of sprayer pipeline wall 2 provided as a filter for exhaust gas, which sewage flow, are filtered according to their degree of contamination of the waste water treatment apparatus using appropriate.

图17~19为有关炼油厂废气燃烧塔废气烟尘过滤装置的实施例构造。 17 to 19 for the exhaust fumes refinery off gas combustion tower constructed embodiment relating to the filtration device. 图17立体示意图中燃烧塔的顶部排气口1周围设有一复数吹风管11,用以辅助排气口处废气能往上升,废气收集壳200为一基本上为由宽渐缩的高壳体,其顶部为一圆筒形烟尘集聚筒202,其两倾侧面设有依序安排的复数喷雾器装设口201,于其宽大底部处连设有一污水收集槽部203,在该烟尘集聚筒202之一侧连接一输气长管2,且该输气长管2亦设有一复数喷雾器装置口28,在输气长管末端接有一污水排放主管261,连接污水收集槽203与污水排放主管261的管路为污水排放支管205,真空泵4的吸入管41与输气管末端一侧连通,且该真空泵4系由一马达3驱动,真空泵4排出管段42连通烟气冷却清洗器210底部。 Combustion exhaust port around the top of the column 1 is provided with a plurality of high-blowing pipe housing 11, the auxiliary exhaust port to be able to rise the exhaust gas, off-gas collection housing 200 is a substantially tapered by the width 17 in perspective view in FIG. , the top of a cylindrical dust accumulation cylinder 202, which is provided with a plurality of sprayers two sides poured sequentially arranged mounting port 201, connected at the bottom thereof is provided with a large water collecting grooves 203, 202 in the cylindrical dust gathering the long side is connected to a gas delivery tube 2, and the gas delivery tube 2 is also provided with a length of a plurality of sprayer apparatus port 28, connected with a water discharge gas transmission competent long tube end 261, 203 connected to the sewage collection tank and sewage competent 261 the conduit 205 is a sewage branch pipe 41 communicates with the pipeline end side of the suction pipe 4 to a vacuum pump, and the vacuum pump system 4 is driven by a motor 3, the bottom of the cooled flue gas scrubber 42 communicates vacuum pump 210 discharge pipe 4. 该输气冷却清洗器210基本上为直立圆筒形,其上端为净气排出管212,其内壁环绕冷气管或冷冻水管211,该烟气冷却清洗器210底部亦连通一污水过滤槽8,该污水过滤槽8一侧底部连接一排水管89,视该排水管89中的水质清或浊的程度,可送至适当的污水处理装置,作进一步的水处理,或直接送至喷雾器利用,污水收集槽部203的底部有一底座601用以固定支持废气收集壳200,输气长管2与污水收集槽203构成了第一阶段废气回收及过滤部分,底座603用以支承烟气冷却清洗器210,烟气冷却清洗器210与污水过滤槽8构成了第二阶段烟气过滤部分。 The cooling gas delivery washer 210 is substantially cylindrical upright, the upper end of which is a net gas discharge pipe 212, the inner wall surrounding the chilled water or cool air duct 211, the bottom of the cooled clean flue gas 210 also communicates a filtered water tank 8, 8 the bottom side of the filter water tank 89 is connected to a drain, the drain pipe 89 depending on the degree of water clear or turbid, can be sent to a suitable waste water treatment apparatus for further treatment, use or direct to the atomizer, sewerage groove bottom portion 203 has a support base 601 for fixing the exhaust gas collecting casing 200, gas delivery tube 2 and the length of the sewage collection tank 203 constitute the first phase of the exhaust gas recirculation and filtration section, a base 603 for supporting the cooled flue gas scrubber 210, flue gas cooling and cleaning stage 210 constitutes a second portion of the smoke filter filtering water tank 8. 底座602则用以固定真空泵用的马达3。 A base 602 for fixing the vacuum pump 3 with the motor.

图18为图17中第一阶段废气回收及过滤部分的剖视示意图。 18 is a schematic cross-sectional view in FIG. 17 and the exhaust gas recirculation filtration part of the first stage. 该图中燃烧塔排气口1仅以截断的方式简示,应用本实施例废气回收装置的燃烧塔高度可大大降低,不必如传统燃烧塔必须竖立至极高处,由于排气口周围完全由废气收集壳200所封闭且收集,故燃烧塔的高度便不是需要加以考虑的问题,一复数的吹风管11连通空气压缩机管路,故由该吹风管离开的空气,有足够的推力将废气上扬至废气收集壳200顶处的烟气集聚筒202,该废气收集壳200倾斜侧部成列设有一复数的喷雾器装设口201,使得诸喷雾器6能适当地被定位及受固持。 The column vent combustion FIG 1 illustrates only cut simple manner, an application example of the combustion exhaust gas recovery tower according to the present embodiment can greatly reduce the height is not necessary as in the conventional combustion tower must be erected extremely high, since the exhaust port is completely surrounded by the gas collection housing 200 is closed and collected, so that it is not the height of the combustion tower issues need to be considered, a plurality of communication with the air compressor blower pipe line 11, so that the air exiting the blowing pipe, the exhaust gas will have sufficient thrust agglomeration barrel 202 up to 200 flue gas at an exhaust gas collection housing, the inclined side gas collection housing portion 200 is provided with a plurality of columns mounted sprayer opening 201, such that the sprayer 6 can be properly positioned and retained by. 由于喷雾器6属固定为习知技术,在此不作详述,输气长管2基本上与本案的输气管2相同,均设有一复数喷雾器6及一复数令水雾四溅的网件20,由于喷雾器6与网件20的固定属现有技术,在此亦不作详述。 Since the atomizer 6 is fixed to the case of conventional art, and will not be described in detail, gas pipe length substantially the same as the case of the pipeline 22, a plurality of sprayers are provided with a plurality of orders and 6 mist scattered mesh member 20, Since the atomizer member 6 and the fixed network 20 is known in the prior art, nor be described in detail herein. 在污水收集槽203内有一成倾斜状的污水收集盘204及与污水排放支管205连接的污水收集口道206,该收集口道206为长形口道,且在与污水排放支管205直接连通处呈收缩成管状,以便污水流下至污水排放支管205,该污水收集槽203可由混凝土制成或其他适当的耐压性高及强度大的材料制成。 There are in the sewage collection tank 203 a inclined shape sewage collection tray 204 and sewerage inlet channel connected to the sewage branch pipe 205, 206, the collection port channel 206 is elongate opening channel, and in direct communication at the sewage branch pipe 205 contracted into a tubular shape, so that water flows down to the sewage branch pipe 205, the sewage collection tank 203 may be made of concrete or made of other suitable high pressure resistance and a large strength material.

图19所示为图17中燃烧塔废气过滤的第二阶段烟气冷却过滤部分剖视示意图。 FIG 19 is a schematic cross-sectional view of the second stage of the flue gas is cooled in the filter portion 17 of the combustion exhaust gas filter column. 以显示其内部构造,当烟气由真空泵4输入烟气冷却清洗器210后,由冷气或冷冻水进口2111处送入的冷气或冷冻水便在冷气或冷冻水输管211中环绕,并从冷气或冷冻水出口2112离开烟气冷却清洗器210,然后该冷气或冷冻水循环到烟气冷却清洗器210中,令其中的温度降至极低,使得轻浮微粒或具毒性的气不致上扬,并且由喷雾器6加以进一步清洗,在该清洗器210中设有网件20,以令水雾能四溅,达到与烟气充分混合,烟气冷却清洗器210底部又接一连通管213,以与污水过滤槽8连接,使得该清洗器210内流下的水液再进入该过滤槽8,利用过滤网206再一次过滤,在该过滤槽8底部邻近处的排水管89可将离开污水过滤槽8的水液送到适当处加以利用。 To show an internal structure, when the flue gas 210 enter scrubber the flue gas is cooled by the vacuum pump 4, the cold air fed by chilled water or cold air inlet 2111 or frozen water or frozen water will cool air delivery tube 211 surrounds, and from or frozen water-air cooling outlet flue gas leaving the cooling and cleaning 2112 210, and the cold air or chilled water to cool the flue gas scrubber 210, so that the temperature therein reduced to very low, so that the particles frivolous or without up-toxic, and 6 to be further cleaned by a nebulizer, with the net member 20 in washer 210, so that mist can be scattered to achieve sufficiently mixed with the flue gas, flue gas cooling and cleaning the bottom of the contact 210 and a communicating pipe 213, with the sewage tank 8 is connected to the filter, so that the liquid water stream 210 within the cleaner re-enters the filtration tank 8, the filter using the filter 206 again, the drain 8 of the filter tank adjacent the bottom 89 of the filter water tank can leave 8 the aqueous solution to be utilized where appropriate.

图17~19所示的实施例系针对单一燃烧塔废气回收及过滤所应用装置,此种回收废气及一再过滤废气的构造,具有极佳的过滤效果,对于多燃烧塔的情况,其回收及过滤装置与燃烧塔回收及过滤装置并无差别,只要将一复数燃烧塔排气口并列,且以多数个输气长管2与真空泵4组合以及多数个烟气冷却清洗器210与污水过滤槽8相组合配以一废气收集壳体200便可达到如图20所示的相同效果。 Embodiment illustrated in FIGS. 17 to 19 for a single combustion system and exhaust gas recirculation filtration column application device, and configured such repeated recycling exhaust gas of the exhaust gas filter having excellent filter effect, in the case of a multi-combustion tower, and recovered and filter means and the filter means combustion recovery column and no difference, as long as a plurality of combustion exhaust ports parallel columns, a plurality of gas transmission and with a long tube 2 in combination with a vacuum pump 4 and a plurality of flue gas cooling and cleaning the filtration tank 210 and the water 8 are combined together with a gas collection housing 200 can achieve the same effect as shown in FIG. 20. 图20所示的剖视图为在壳体200内有三个燃烧塔排气口101、102及103及其周围的吹风管组111、112及113并列一起的布置形式,该三个排气口101、102及103亦被一较大范围的废气收集壳200所封闭的实施例,事实上,多燃烧塔排气回收与过滤装置是单燃烧塔排气回收与过滤装置的放大与叠加便可构成相应的回收与过滤功效。 20 a cross-sectional view shown in FIG hair is tube group 111, 112 113 and three exhaust ports 101 and the combustion tower 103 and its surrounding in parallel with the arrangement in the housing 200, the three exhaust ports 101, 200 Example 102 closed and 103 were also a wide range of off-gas collection housing, in fact, multi-column combustion exhaust gas is recovered with a single filtering device amplifies the combustion exhaust gas recovery and superimposed on the filtering device can be configured corresponding column recovery and filtration efficiency.

图21为本过滤系统中应用于过滤污浊空气的烟尘过滤装置的一实施例的剖视示意图;其中该输气管2中除设有喷雾器6,网件20的外,又设有吸尘装置41,刷件式挡水器51,且输气管2较短而其前端螺固有网盖1,由吸尘装置的运转而将污浊空气引入,以便清洗过滤污废的空气,通过一复数网件20的空气仍含有许多水份,再经刷件式挡水器5,使得水份不会混在空气中离开输气管2,出气端所设置的抽风扇4及驱动马达3,于本实施例的输气管2中则视吸气装置41对污浊空气抽吸容量的大小,而使其运转或不运转;也就是吸尘装置41的抽吸能力极强或污浊空气的污浊浓度不高时,则仅运转吸尘装置41即可流至输气管2底部的污水经排水管口26排出并可运通至轻便式污水处理装置(参见图42及图43)中,加以过滤及回收。 FIG filtration system 21 of the present filter is applied to the soot filter dirty air schematic sectional view of a device according to the embodiment; wherein the pipeline 2 in addition to a sprayer 6, the outer member web 20, and the suction device 41 is provided brush retaining piece 51, and a shorter pipeline 2 with its front end cap 1 screwed inherent network, and the operation of the suction device is introduced from the dirty air, in order to clean the air filter waste and sewage through a complex web member 20 the air still contains a number of water, and then the brush retaining piece 5, so that water will not be mixed in the air leaving the pipeline 2, the outlet end of the suction fan is disposed a drive motor 3 and 4, the present embodiment of input in the pipe 2 depending on the size of the 41 pairs of dirty air suction capacity of the suction device, while it is not operating or operate; i.e. when the suction capacity of the suction device 41 is extremely dirty or not dirty air concentration is high, only the operation of the suction device 26 can be discharged to the bottom of the pipeline 41 flows through the sewage drain port 2 and transported through sewage treatment plant to a portable (see FIG. 42 and FIG. 43), it is filtered and recovered. 本输气管2与轻便式污水处理装置均可制成可移动式的,而非固定于一处,在图19中未将可移动的元件给出,由于其为现有技术,故不再阐述。 This sewage pipeline 2 and the light treatment device can be made movable, rather than a fixed, non-movable element is given in FIG. 19, since it is prior art, it is not described .

图22、图23及图24分别用以表示吸尘装置与扩散水雾的网件20回定的情形,吸尘装置41基本上为具长方体框架的吸抽马达组合的装置,其中包含一复数风扇马达组合411,图23所示的风扇马达组合411为四组,每一风扇马达组合411均有适当的固持件412固定,图22及图23所示固持件412仅系示意性质,其为现有技术,不再阐述。 22, 23 and 24, respectively, to indicate the suction device and the web member 20 back diffusion of mist given situation, suction device 41 is substantially rectangular parallelepiped frame having withdrawing means pumping motor assembly, which comprises a plurality of the fan motor assembly 411, as shown in FIG. 23 of the fan motor assembly 411 into four groups, each of the fan motor assembly 411 has a suitable fixing holder 412, as shown in FIG. 22 and FIG. 23 holder 412 illustrative nature only and which is the prior art, not described. 吸尘装置41的四个直角端分别固定在四个等长杆形固定件7的前端部附近,各杆形固定件7后端部附近则固定有一复数网件20,各网件外围连有固定环201,而此固定环201的外周围便可固定至各杆形固定件7上,图21及图22上仅表示二个网件20的示意图,实际上应用时,可依需要而增加或减少,并非定数,四杆形固定件7的长度短于输气管2中由前端口至锥形渐缩段的起始处,即各杆形固定件7系被定位于输气管2的前端口后至锥形渐缩段的起始处前的位置,各该杆形固定件7的外侧表面与输气管2的内壁形成套合接触状态,参见图23和图24。 Four right-angle end of the suction device 41 are fixed to the front end portion in the vicinity of four equally long rod-shaped fixing member 7, 7 near the rear end portion of the bar-like fixing member 20 is fixed, a plurality of network elements each network element is connected with a peripheral fixing ring 201, and this outer periphery 201 of the securing ring can be fixed to each of the bar-like fixing member 7, a schematic view of two web members 20 and 22 of FIG. 21 only showing, in fact, when applied, can also need to increase or reduction is not a fixed number, four shaped fixing member 7 is shorter than the length of the pipeline 2 at the beginning by the first port to the conically tapering section, i.e., bar-like fixing member 7 is positioned at the front line of the pipeline 2 after conically tapered port to a position before the beginning of the segment, each of the bar-like fixing member and the inner wall surface of the pipeline 2 7 formed on the outside of the nested contact state, see FIG. 23 and FIG. 24. 因此,当欲维护保管吸尘装置41及网件20时,可将各该杆形固定件7拉出以与输气管2的壳体分离,为稳固杆形固定件7于输气管2中,可设一复数的习用固持件于适当位置,以便达到杆形固定件7的稳固效果。 Thus, to be maintained when the storage device 41 and the suction member 20 o'clock network, each of the rods may be shaped fixing member 7 pulled out of the housing and the pipeline 2 was isolated as a solid bar-like member 7 is fixed to the pipeline 2, It may be provided a plurality of conventional holder in place, in order to reach a solid bar-like fixing member 7 by the effect.

图25及图26为针对挡水器部分加以说明,挡水器由一固定环板51,挡水刷组合53组成,该固定环板51外径相等于输气管2的外径,以便能定位于输气管2上,于该固定环板51上固定有一复数垂直且成间隔的挡水刷组合53,挡水刷组合53中的各垂直刷件的长度略等于依其固定在固定环板51的位置及固定环板51外径所构成而形成的弦长,固定环板51顶面适当处设有把手52,以便将挡水器放置于输气管2上或自输气管2取下。 25 and FIG. 26 will be described for the retaining portion, the retaining ring consists of a fixing plate 51, a combination of retaining the brush 53. The fixing plate 51 the outer diameter of the ring is equal to the outer diameter 2 of the pipeline, in order to be positioned 2 to the pipeline, on the fixing ring 51 is fixed to a plate and a plurality of vertically spaced retaining into the brush 53 in combination, the combined length of each vertical brush retaining member of the brush 53 is roughly equal to the fixed plate in accordance with its fixing ring 51 chord position and the outer diameter of the fixed ring plate 51 is formed constituted of the appropriate surface of the fixed ring plate 51 is provided with a handle 52 for retaining the pipeline 2 is placed in or removed from the pipeline 2.

图27所示为图25中挡水器51放置在输气管2上的输气管2的侧视示意图。 Figure 27 is a drawing 2551 waterdam pipeline 2 is placed on the pipeline 2 is a schematic side view. 以表示挡水器的放置位置,在输气管2锥形渐缩段的起始处前有一弧形缺口25,用以令挡水器置于其中,而挡水器的两侧端54定位于缺口25的底部壳体部251处。 To indicate the placement of the retaining device, before the start of the pipeline 2 is conically tapered section has an arcuate cutout 25, which is placed to make the retaining, and the both side ends of the retaining device 54 is positioned at the bottom of the notch 25 of the housing portion 251. 由图26中也可看出挡水器定位的情形。 In the case of FIG. 26 can also be seen that a mist eliminator positioned. 图28所示为挡水器上挡水刷组合53后可依需要增加一列挡水刷组合531,构成二列挡水刷组合的情形,甚至于可设置三列以上,其主要目的为阻挡水份,但不能因多列挡水刷组合的设置而阻凝净气的行进。 Figure 28 is a combination of a mist eliminator brush can also need to increase retaining a retaining brush 531 after composition 53, constituting retaining case two brush combination, and even more than three may be provided, which primary purpose is to block water parts, but can not be provided because of the combination brush retaining a plurality of columns and traveling gas barrier net condensate.

图29所示为设于输气管前端的网盖1的B向示意图,用以令输气管2与外界隔开,以达运转时的安全,该网盖1的外围为固定环板11,且于固定环板11的邻近外周围处,设有一复数的等角小螺孔12,以便与输气管2前端口的边缘以螺栓27固定一起,如图21所示的螺固状态。 Figure 29 shows a mesh provided at the front end of the pipeline 1 to the schematic cap B to make the pipeline 2 from the ambient, to reach the safety of operation, the web is a peripheral cover plate fixing ring 11, and adjacent the outer periphery of the fixed ring plate 11 is provided with a plurality of small holes equiangularly 12, 27 so as to be fixed with screws to the front edge of the port pipeline 2, 21 screwed state shown in FIG.

图30为各喷雾器6装置于输气管2上的情形,在同一输气管2断面所装设的喷雾器数量可依等角距间隔设置。 FIG 30 is a case where each of the sprayer 2 to the pipeline means 6, the number of sprayer 2 is mounted in the pipeline section to follow the same pitch at equal angular intervals.

图31至图33系表示烟尘收集器第一实施例外部的构造图。 31 to 33 are diagrams of the first embodiment of dust collector portion exception configuration of FIG. 对于废气中含有多量颗粒状烟尘的情况时,要先将较粗微粒收集后,再令离开收集器的烟气进入烟尘过滤装置以减轻烟尘过滤装置运滤负荷,请同时参阅图31~33,烟尘收集器部分主要由一烟尘收集筒3,二个水滴收集槽33,一渗水网32,一烟尘抽吸管4,一烟尘抽吸泵41,一转轴传动装置7,以及一转轴支持架组62等构件组成,烟尘收集筒3的筒腹前侧靠近两端处各设有一人孔31,以便用以检视收集筒3内部或执行维修工作,渗水网32系覆在收集筒3的上半部筒腹,用以冷却及促进散发收集筒筒腹热量,二水滴收集槽33均为长形顶部散开且底部有一流放口的槽,分别固定于收集筒3下半部筒腹两侧适当处形成对称部置,其固定方式系应用一般习知焊固或螺固或其他合适方式,收集筒3左端面为一复数的冷气输送口35,该冷气输送口35上各有一开口调整片,用以调整 For the case where the exhaust gas contains a large amount of particulate dust, coarse particles will be collected first, then make the flue gas leaving the dust collector into the filter means to reduce operation load of the soot filter filtration apparatus, Referring to FIGS. 31 to 33, dust collector portion mainly composed of a dust collection cylinder 3, two droplet collection tank 33, a seepage network 32, a dust suction tube 4, a dust suction pump 41, a drive shaft 7, and a shaft holder group like member composed of an upper half 62, close to the fume collection tube at both ends of the ventral side of the front cylinder 3 is provided with each one hole 31, so as to view the collection tube 3 within or maintenance work, seepage-based network 32 overlying the collection tube 3 abdominal tube portion to facilitate distributing and collecting cooling cylinder tube heat abdomen, two droplet collection tank 33 are elongated groove and the top of a disperse exiled bottom opening, the collection tube 3 are fixed to the lower half of the cartridge abdominal appropriate sides formed at symmetrical section facing, fixed manner based applications are generally conventional welding solid or screwing or other suitable means, the collection tube 3 the left end surface of a plurality of cool air delivery port 35, the cold air delivery have an opening tab 35 opening, to adjust 冷气输送口35的开口大小,而且,该等冷气输送口35的开口方向均不会相同,使得流入收集筒3的冷气具有扰动烟尘且冷却烟尘的效果,因冷气管路与收集筒3连通的构造为已知技术,故省略。 Cool air delivery opening size of the opening 35, and, the direction of such air-delivery opening port 35 are not the same, so that the cool air flows into the cylinder 3 has collected and cooled smoke dust disturbance effects due to the cold air conduit communicating with the collecting tube 3 configured to known art, it is omitted. 收集筒3右端为封闭端,仅有令其内部的旋转轴34伸出,以与转轴传动装置7连接,该转轴传动装置7为一受速齿轮箱及传动马达的组合构造,或其他适当的机械传动构造,也为已有技术,不再阐述。 Collecting cylinder 3 is closed right end of the rotary shaft 34 so that it only extends inside, with the shaft connected to transmission means 7, the drive shaft is configured as a combination of a 7-speed gearbox and transmission by a motor, or other suitable mechanical transmission structure, but also for the prior art, not described. 在转轴传动装置7的下方为一固定该装置的支持座61、转轴34的左端则为一轴承座621,且该轴承座621固定于转轴支持架62上,烟尘收集筒3的下方密接烟尘抽吸管4,该烟尘抽吸管4被一复数的固定环42或相同功能的固定件固定在收集筒3上。 Below the drive shaft 7 is fixed to a support base 61 of the device, compared to a left end of the rotary shaft 34 of the bearing housing 621 and the bearing housing 621 is fixed to the shaft holder 62, the adhesion of smoke dust collected below the pumping cylinder 3 suction pipe 4, the dust suction pipe 4 is fixed a ring 42 or a plurality of the same functions as the fixing member 3 is fixed on the collecting cylinder. 该烟尘抽吸管4末段装设烟尘抽吸泵41,在烟尘抽吸泵41末端开口套接一滤袋81,当烟尘进入该滤袋81时,藉由滤袋81的具可透气性及可伸缩性,令颗粒烟尘滞留于袋中,由于烟尘抽吸泵41,也为现有技术,故不再叙述。 The dust suction pipe end section 4 is mounted fume suction pump 41, suction pump 41 end of the dust bag opening a socket 81, when smoke enters the filter bag 81, with bag 81 with gas permeability and scalability, so that the soot particles are retained in the bag, since the smoke suction pump 41, but also for the prior art, and therefore will not be described. 一烟气连管10之一端连至收集筒3右端后侧筒腹中部,另一端连通烟尘过滤装置,使得由该烟气连管10离开收集筒3的烟气进入烟尘过滤装置中,参见图33至图34,由烟尘过滤装置流出的污水经由烟尘过滤装置排水口下流至污水容纳槽80,在污水容纳槽80前侧底部处设有一复数供水歧管803,该等供水歧管803的末端又接一滴水横管802,且该滴水横管802有一复数的滴水孔,使来自供水歧管803水液能往上滴至收集筒3上所覆盖的渗水网32上,藉以冷却及散发收集筒3表面的热量,经由渗水网32流下的水则经由二水水滴收集槽33被送至污水处理装置。 A flue gas pipe connected at one end connected to the collector 10 of the right rear cylinder barrel 3 belly portion, the other end of the communication soot filter means, such that even the tube 10 away fume collection cylinder 3 by means of the flue gas into the particulate filter, referring to FIG. 33 to FIG. 34, the sewage flowing out from the filter dust from the dust filter means via the drain water flows down to the receiving groove 80, is provided with a plurality of supply manifold 803 in the receiving groove 80 before the sewage at the bottom side, the end of these supply manifolds 803 a drop of water and then cross pipe 802 and the pipe 802 has a cross-drip dripping a plurality of holes, so that liquid water pipe 803 from the water supply manifold could drop up to the upper collecting tube 3 is covered seepage network 32, thereby distributing and collecting cooling heat the surface of the cylinder 3, the collection tank 32 via the network flow seepage water droplets 33 is sent via dihydrate sewage treatment apparatus. 由于渗水网32滞留了一部分烟尘,所以流至水滴收集槽33的污水浓度已较轻,故可直接送至简便式滤袋污水处理装置,参见图42至图43。 Since a part of seepage soot retention net 32, so that the water droplets flow to the sewage collection tank 33 has a lesser concentration, it can be sent directly to the bag-type waste water treatment apparatus is simple, see FIGS. 42 to 43. 若流至水滴收集槽33的污水浓度仍高,可考虑以迂回式滤袋污水处理装置作为污水处理作业装置,各供水歧管803可藉由一固定架63固定,因各固定架63也为现有技术,故不再赘述。 If the droplet flows to the sewage collection tank 33 remains high concentration, may be considered to circuitous bag sewage treatment plant as a sewage treatment operation means, each supply manifold 803 by a bracket 63 may be fixed, because each of the holder 63 is also the prior art, and therefore will not be repeated. 污水容纳槽80左侧上端附设一污水溢流管801,当污水容纳槽80中的水液溢流时,该污水溢流管801能将溢流出的污水送至适当污水处理装置。 An upper end 80 attached to a left side of the sewage water receiving tank overflow pipe 801, when the water in the water receiving fluid overflow tank 80, the sewage can overflow the overflow pipe 801 to the sewage treatment apparatus suitable sewage. 在污水容纳槽80底处亦有一固定座64,见图33,以稳定该污水容纳槽80。 Also has a holder 64 at the bottom of the water receiving groove 80, shown in Figure 33, to stabilize the water receiving groove 80.

图34所示为烟尘收集筒3与部分烟尘抽吸管4的剖视图。 34 and FIG. 3 a sectional view of the soot portion of the suction pipe 4 is drawn fume collection tube. 以观察该收集筒3内部的诸构件及烟尘抽吸管4与收集筒3的连接情形,首先转轴34上固设有一复数的烟尘附着板组36,在各该附着板组36上的每一附着板36上均有二直立长孔362,以使两相对的滑条361可贴附并卡夹在直立长孔362中。 To observe the interior of the collection tube member 3 and various dust suction duct 4 connected to the case 3 and the collector cylinder, the first shaft 34 is provided with a plurality of the solid dust attachment plate group 36, each on each of the attachment plate 36 of the group Each plate 36 is attached on two vertical long hole 362, so that the two opposing slide bar and clip 361 may be attached in an upright long hole 362. 并能沿着该二直立长孔362作径向的往复移动,使得附着板上的烟尘可被该二滑条361刮除,在转轴34上又固定有一复数的轴环371,各轴环371上有相距180度的二径向杆37,复数轴环371与二径向杆37组合后被设置在各烟尘附着板组36右侧或左侧邻近处。 362 and can reciprocate radially along the two vertical elongated hole, so that the dust can be attached to the plate 361 two scraper slider, and is fixed on the rotary shaft 34 has a plurality of collar 371, the collar 371 each there are 180 degrees apart on two radial rods 37, a plurality of collar 37 in combination with a dicarboxylic 371 radially disposed in the fumes after attachment plate group 36 adjacent to the right or left. 各径向杆37末端均固设有一压缩弹簧372,而各压缩弹簧372的另一端则分别被固定在二横向长刮条38的内侧边,各径向杆37的长度小于收集筒3内径,由于各轴环371本身具有一厚度以及各压缩弹簧372的弹力,使得二长刮条38的外侧边可以与收集筒3的内壁面接触,尚且该二长刮条38的长度均被设成约略相等于收集筒3的内壁轴向长度,因此,附着在收集筒3内壁的烟尘,会因转轴的旋转而被二长刮条38所刮除,所以滑条361地烟尘附着板36的烟尘刮除及长刮条38对收集筒3内壁的烟尘刮除均有效地达成。 Each radial end of each rod 37 is provided with a compression spring 372 fixed, while the other end of each compression spring 372 is respectively fixed to the inner length of the wiper strip 38 two transverse edges, each of the radial length of the rod 37 is smaller than the inner diameter of the collection tube 3 , since the elastic force of the collar 371 itself has a thickness, and each of the compression springs 372, so that the two long sides of the wiper strip 38 can be the outside contact with the inner wall surface of the collection tube 3, yet the length of the wiper strip 38 are provided two long roughly equal to the axial length of the inner wall of the collection tube 3, and therefore, the dust collector attached to the inner wall of the barrel 3, due to rotation of the long shaft is two scraper wiper strip 38, so that slider 361 is attached to plate 36 dust dust wiper strip 38, and long scraping soot collection tube inner wall 3 of the blade are effectively reached. 在收集筒3底部处间隔地设有一复数落尘出口39。 At the bottom of the barrel 3 is provided with a plurality of collected dust outlet 39 at intervals. 烟尘抽吸管4相对于各落尘出口处亦设有一复数落尘吸入口43,以便抽吸泵41运转时落尘可经由各落尘出口39及各落尘吸入口43而被抽至滤袋81中。 Dust suction tube 4 with respect to the dust outlet of a respective drop also has a plurality of dust suction port 43, so as to suck dust may be the pump 41 operated by the dust outlet 39 and all dust suction port 43 is drawn into the filter bag 81. 有关二滑条361的连结情况及落尘出口39与落尘吸入口43的连通情形,将在图35与图36中加以详述。 Dust outlet coupling case and the slide 361 about two dust intake 39 and the communication port 43 of the case, which will be described in detail in FIG. 35 and FIG. 36.

图35为图34的AA剖视图。 FIG 35 is a cross-sectional view AA of Figure 34. 由该图可清楚看出各烟尘附着板36等角距离地固定在转轴34上,各烟尘附着板36上的二滑条361系以固定销固定或以具相同功能固定件活动夹固并沿361径向作往复滑动在直滑槽362上。 Apparent from this figure, each of the dust attachment plate 36 is fixed equal angular distances on the shaft 34, two slider on 36361-based or a fixed pin secured to the fixed member having the same function as each of the active clamp and fumes along the attachment plate 361 reciprocates radially slidable on a linear chute 362. 由于各烟尘附着板36上二滑条361为分别贴面至各附着板36的二外表面,故可对该烟尘附着板36作烟尘刮除操作。 Since the dust attached to each of the two slide plates 36 are affixed to the surface 361 to the outer surface of each of two of the attachment plate 36, so that the wiping operation can be used for smoke fumes plate 36 is attached. 图36为图34的BB剖视图。 FIG 36 is a cross-sectional view BB of Figure 34. 由该图可以清楚看出轴环371套于转轴34上,其套固的方式可为键与键槽方式或固定螺丝螺固方式,或其他具固定功能的方式,因它现有技术,故在图中未示出。 As apparent from the graph of the collar 371 on the sleeve shaft 34, which sets solid way keys and the keyways may be set screws or screwed manner mode, or other mode with a fixed function, because it is prior art, so in not shown in FIG. 二径向杆37则成180度的角距离布置,而二长刮条38则与收集筒3的内壁保持浮顶接触,落尘出口39与落尘吸入口43的间系以套接密合方式连通,以便于抽吸泵41能有效将落尘经抽吸管4而至滤袋81中。 Two radial rods 37 into an angular distance of 180 degrees is arranged, and two long wiper strip 38 is maintained floating roof in contact with the inner wall of the collection tube 3, dust outlet 39 and the dust suction port 43 intersystem communication with socket adhesion manner , so that the effective suction pump 41 via the dust suction pipe 4 and to the filter bag 81.

图37为图31中滤袋81的内部构造图。 FIG 37 is an internal configuration diagram of the filter bag 31 in FIG. 81. 该图中显示滤袋81可分为外层811,中层812及内层813,它们由连接带814及补强带815将各层连固一起,滤袋81的材料为具可透气性且可伸缩性的纤维质构成,尚且内层部分的网目8131较大,中层部分的网目8121较小,外层部分的网目8111最小,使得较粗颗粒烟尘滞留于内层袋813,次粗颗粒烟尘滞留于中层袋812,最细的烟层滞留于外层袋811,使其能有效过滤被抽吸的混合烟尘的废气。 Display 81 can be divided into an outer bag 811, the middle layer 812 and inner layer 813 in FIG., They are connected by a belt 814 and reinforcing belt 815 to connect the layers together with a solid material having a bag 81 is air permeable and can stretchable fibrous structure, yet mesh inner portion 8131 is large, a smaller middle portion 8121 mesh, mesh minimum outer portion 8111, so that coarser particles of soot accumulated in the inner bags 813, roughing soot particles are retained in the bag middle 812, the smallest tobacco retained in the outer layer of the bag 811, so that it can effectively filter the exhaust gas is sucked in the smoke mixing.

综合图31~37所述内容,烟尘由排气管1先进入烟尘收集筒3,此时转轴34亦已转动,由收集筒3左端进来的冷气一方面扰动收集筒3内部的烟尘,一方面冷却收集筒3内部的高热气体,烟尘因收集筒3温度降低,而减缓飞扬活动,并且附着在收集筒3内壁上与烟气附着板36上,滑条361与长刮条38便分别刮下烟尘附着板36与收集筒3内壁上的烟尘,并由收集筒3底部进入抽吸管4,最后被吸入滤袋81,离开收集筒3的烟气则经由烟气连管10进入烟尘过滤装置2中接受过滤,由烟层过滤装置底部排水口出来的污水则经由污水容纳槽80,供水歧管803及滴水管802滴至收集筒3的上表面,以散发收集筒3表面上的热量,使得收集烟尘功效更能提高。 The FIGS. 31 to 37 integrated content, fume exhaust pipe 1 into the first dust collecting cylinder 3, the shaft 34 has also rotated at this time, the inside of the dust collected by the collecting tube 3 cylinder 3 left cold air coming aspect disturbances, on the one hand cooling the interior of the collection tube 3 heat the gas, dust collecting cylinder 3 due to temperature decreases, and the slow flying activities, and adhered to the inner wall of the collection tube 3 and the upper plate 36 attached to the flue gas, and the long slider 361, respectively, the wiper strip 38 will be scraped soot and dust attachment plate 36 on the inner wall of the collection tube 3, the bottom of the barrel 3 by collecting into the suction tube 4, and finally is drawn into the bag 81, the flue gas leaving the collection cylinder 3 is connected via a flue gas pipe 10 enters the soot filter means receiving filter 2, the drain water out of the bottom of the device via the layer of smoke is filtered by the sewage holding tank 80, the water supply manifold 803 and the tube 802 drops drip onto the surface of the collection tube 3, to dissipate heat on the surface of the collection tube 3, so that can enhance the effectiveness of collecting dust.

图38为一种滤袋或污水处理装置8,用以将烟尘过滤装置所流下的水作一过滤。 FIG bag 38 as a waste water treating apparatus or 8 for the particulate filter apparatus for water flowing down a filter. 本滤袋过滤装置中有数个连接烟尘过滤装置2底部的污水流出管25的污水连管251,各污水连管251又与一横向连管252连接,该横向连管252又与一复数L形短歧管253连通,各短歧管末端则分别固定一长形滤袋81,诸过滤袋81的直接下方则为一长形大集水槽83,于该集水槽83下连有数个下流管84,经由滤袋流出的水液能被送至水液处理装置101,参见图39。 This bag filter apparatus with several soot filter means connected to the bottom of the sewage flowing out of the tube 2 sewage pipe 251 is connected to 25, each of the sewage pipe 251 is connected in turn connected to a transverse link tube 252, the transverse link tube 252 with a plurality of L-shaped and short manifolds 253, each short end of the manifold are secured an elongate filter bag 81, such filter bags 81 directly beneath the elongated, compared with a large sump 83, is connected to the collection tube 84 under several downflow sink 83 , via the water flowing out of the liquid bag can be supplied to aqueous liquid processing apparatus 101, see Fig 39. 在集水槽83中置有一面积略小于其底部面积的支持网件82,用以支持各滤袋底部,避免复数的滤袋悬空不稳定,滤袋81本身材质可利用具伸缩性的纤维质,具有数层的过滤层,如图37所示的滤袋亦极适合应用于此。 In the sump 83 placed thereon with a bottom area slightly smaller area network support member 82 to support the bottom of each bag, to avoid the complex unstable vacant bag, the bag material 81 itself may be utilized with a stretchable fiber, several layers having a filter layer, the filter bag 37 as shown in FIG electrode also suitable for this. 滤袋81的袋口可以绳索固定,或以其他适当固定方式亦可,当滤袋81充满被过滤的烟尘,亲质等后,可以方便取下,并换上一新过滤装。 Pocket bag 81 may be fixed rope, or other suitable fixing means may, when the filter bag 81 is filled with dust, and other pro-quality, can be easily removed and replaced with a new filter device. 由于各短歧管253上均设有一止水阀254,以便更换滤袋时,可将其关闭,以防污水流出。 Since each short upper manifold 253 has a sealing valve 254, so that when replacing the bag, it may be shut down to prevent water outflow.

图39为一水液处理装置的实施例,可将滤袋过滤装置8下流管84中的水液加以处理。 Figure 39 is an embodiment of the liquid processing apparatus of water, bag filter means may be aqueous 8 downpipe 84 to be processed. 经过滤袋过滤装置8的水液,应属较清洁水液,为使该水液更为清洁,以便能再回收利用,本水液处理装置101便扮演重要角色。 After filtration device aqueous bag 8, it should be relatively clean aqueous fluid, such that the aqueous liquid cleaner for recycling again, the present aqueous liquid processing apparatus 101 will play an important role. 本水液处理装置101基本上由一搅拌槽1011,数个沉淀槽1012,以及一清水槽1013串连结成,各槽体均为长方形断面,而各槽的容积,可依实际需要而定。 This essentially aqueous liquid processing apparatus 101 by a stirring tank 1011, a plurality of the precipitation tank 1012, and 1013 in series to form a clear water tank, each tank section are rectangular, and the volume of each groove, to follow the actual need . 搅拌槽1011主要接受下流管84的水液,并且有一常用的搅拌器11设置在该槽中,以便令水液被充分搅和,不会沉淀。 1011 stirred tank main recipient aqueous downpipe 84 and a conventional agitator 11 arranged in the groove, in order to make mix is ​​sufficiently liquid water, does not precipitate. 搅拌槽1011与其相邻的沉淀槽1012间,以及相邻的两沉淀槽1012间,以及最后一个沉淀槽1012与其清水槽1013间的适当处均设有流通孔1014,使得搅拌槽1011的水液能依次流经所有沉淀槽1012,最后水液达至清水槽1013处时,已属更清洁的水。 1012 1011 stirred tank adjacent thereto sedimentation tank, and 1012 between the adjacent two sedimentation tank, and a final precipitation tank 1012 at its proper clearance between the water tank 1013 has flow holes 1014, so that the water was stirred tank 1011 can sequentially through all the precipitation tank 1012, the time to reach the final aqueous clean-water tank 1013, already more clean water. 在各沉淀槽底部均放置一污物附着板14,该附着板14面积可覆盖各沉淀槽的整个底部面积。 The bottom of each settling tank are placed dirt attached a plate 14, the attachment plate 14 may cover the entire area of ​​the bottom area of ​​each sedimentation tank. 清洗槽1013中设有一个或数个抽水管12,可将清水槽1013中的水抽离并再回收至强力喷雾器组6中,以便循环利用。 The washing tank 1013 is provided with one or several of the suction pipe 12 can be pulled clean water tank 1013, and recycled to the strong nebulizer group 6, for recycling. 若强力喷雾器组所喷出的水雾系石灰水、肥皂水、或其他适当清洗剂,由抽水管12抽离的水,必须先混以石灰粉、肥皂或其他适当的清洗剂,再由强力喷雾器组喷出。 If the strength of the ejected mist nebulizer group lime-based, soapy water, or other suitable cleaning agent, a water suction pipe 12 is pulled out, must be mixed with lime powder, soap or other suitable cleaning agent, then the strong atomizer discharge group. 清水补助管9与设于补助管9末端处的浮球阀90装于清水槽1013中,以尔补清水槽中的水量,以供抽水管12的抽吸。 Water pipe 9 is provided in the grant grants float valve 9 at the end of the tube 90 is mounted on the clean-water tank 1013, Seoul fill water to the water tank, the suction for the suction pipe 12. 在清水槽1013的顶部边侧附近,设一溢水管13,以便溢出清水槽1013中过量的水。 Near the top side of the clear water tank 1013, an overflow pipe 13 is provided so as to clear the overflow of excess water in the tank 1013.

图40与图41所示为水液处理装置101的另一实施例。 40 and FIG. 41 is another aqueous liquid processing apparatus 101 illustrated embodiment. 本水液处理装置101的槽体为圆筒形,以取代长形槽。 This aqueous solution tank processing apparatus 101 has a cylindrical shape, instead of an elongated slot. 在搅拌槽1011中设有一支架板110以固定搅拌器11。 It is provided with a support plate 110 fixed to the agitator 11 in the stirring tank 1011. 与图39的水液处理装置相同,由于滤袋过滤装置流出的水液,经流出管84进入搅拌槽1011,再经流通孔1014流入数个沉淀槽1012,最后进入清水槽1013,再由抽水管12将水抽离并再循环利用。 The same aqueous liquid processing apparatus of FIG. 39, since the liquid water flowing out of the filter bag, through the outflow pipe 84 into the mixing tank 1011, and then flows through a plurality of flow holes 1014 precipitation tank 1012, and finally into the clean-water tank 1013, and then by pumping the water pipe 12 detached and recycled. 整个处理装置101中所有构件与图39的长形处理装置完全相同,极为适合占地空间有限的情况。 The entire processing apparatus 101 in the processing means for all the elongate member 39 is identical, very suitable where floor space is limited. 图41是图40的A向局部剖视图。 FIG 41 is a partially cross-sectional view A of FIG. 40.

此外,图42与图43所示为简便式滤袋污水处理装置实施例的构造图。 Further, FIG. 42 and FIG. 43 showing an example of configuration of a simple formula for the bag sewage treatment apparatus embodiment. 该简便式滤袋污水处理装置主要由一箱体80、一滤袋81、一集水板82、一多孔隔板83、二高压喷雾机84及85、一中央隔板86、一过滤夹层87,以及一浮球控制阀90所构成,原案的输气管底端的排水管25被接至箱体80顶部一侧,且排水管25的末端伸入箱体80中,使得滤袋81的袋口能固定在排水管25的末端处,图中滤袋81的袋口系以绳带811固定在排水管25的末端,但亦可用其他适当的习知固定方式,滤袋81的材质系透水性与具伸缩性材料,因此可令水液通过而阻挡污尘离开滤袋81,集水板82上有一集水口821对正滤袋81下方,于是由滤袋81流下的水液便经该集水口821流至箱体80的下部左侧,箱体80下部左侧的水液则穿过设于箱体80下部中央处附近的多孔隔板83,并经介于多孔隔板83与中央隔板86之间的过滤夹层87,由于中央隔板86下半部为多孔板部861,因此在箱体80下部左侧 This simple formula bag by a sewage treatment apparatus main housing 80, a bag 81, a water-collecting plates 82, a porous separator 83, two high-pressure sprayers 84 and 85, a central partition 86, an interlayer filter 87, and a float control valve 90 is constituted, the original bill bottom drain 25 is connected to the pipeline 80 side of the top of the tank, and the drain terminal 25 extends into the housing 80, so that the bag 81 bag can be fixed at the mouth end of the drain pipe 25, the bag system 81 in FIG bag 811 is fixed to the cord at the end of the drain pipe 25, but also by other suitable conventional fastening means, the material-based water-permeable bag 81 and exemplary of stretchable material, can make the aqueous barrier by dust and dirt away from the filter bag 81, the water-collecting plate 82 has a downward outlet 821 pairs of the positive current collector bag 81, the bag 81 so the flow from it through the aqueous solution flow collector outlet 821 to the left of the lower case 80, left lower aqueous box 80 is provided in the housing 80 through the lower portion of the porous separator 83 near the center, and by the porous separator 83 interposed between the central filtered interlayer 87 between the separator 86, the separator 86 due to the lower half of the central portion 861 is a porous plate, and therefore the lower left side in the housing 80 水液又再经一次过滤而达至箱体80下部右侧,第一高压喷雾机84与第二高压喷雾机85分别设置于箱体80上部右侧,第一高压喷雾机84位置高于第二高压喷雾机85的上,且两者分别由座板843与853支持及固定,利用第一高压喷雾机84的吸水管841及出水管842以及第二高压喷雾机85的吸水管851及出水管852,将过滤后的水液送至烟尘过滤装置的喷雾器组中,以执行清洗及过滤烟尘工作。 Aqueous solution was once again filtered and the casing 80 to the lower portion of the right side, a first high-pressure sprayer 84 and the second high-pressure sprayers 85 are provided on the right side of the upper housing 80, a first high-pressure sprayer 84 position higher than the first the two high-pressure sprayers 85, respectively, and both the seat 853 and support plate 843 and fixed, using a high-pressure sprayer a first suction pipe 841 and outlet pipe 84 of high-pressure sprayer 842 and the second suction pipe 851 and the 85 pipe 852, the aqueous solution filtered to the soot filter group nebulizer device to perform the work of cleaning and filtering dust. 在箱体80右侧下部设有的供水管9与水源连接,而在供水管9末端装设一浮球控制阀90,当箱体80下部右侧水位降低时,浮球控制阀90便令供水管末端打开,加入水液至箱体80下部右侧,以供给第一及第二喷雾机84及85有足够水液可抽吸,箱体80前侧有一箱门801,参见图43。 The right side of the lower housing 80 is provided with a water supply pipe 9 is connected, in the end of the water supply pipe 9 is mounted a float control valve 90, the housing 80 decreases when the right lower water level, the float 90 has made the control valve open end of the water supply pipe, water was added to the solution right lower casing 80, is supplied to the first and second sprayers 84 and 85 have sufficient aqueous smokable, the front side of the housing 80 has a door 801, see Figure 43. 该箱门801上设有把手802,且该箱门801可以铰链803固定于箱体80上,以便于利用箱门801的开启,而进行本简便式污水处理装置内部构件的维修,以上所述的简便式滤袋污水处理装置,兼具污水过滤与水液处理功能,极适合污浊程度较轻的污水处理。 Provided with a handle 801 on the door 802, the door 801 and hinge 803 can be fixed to the casing 80 so as to open the door using the 801, while the maintenance of the inner member of this simple type sewage treatment apparatus, described above simple bag-type waste water treatment apparatus, both filtered water and aqueous solution processing, the degree of contamination of the lighter is very suitable for waste water treatment.

综上述的烟尘过滤装置2,滤袋过滤装置8,以及水液处理装置101,可知本发明的污浊气体过滤系统,首先以烟尘过滤装置2将污浊气体或高压气体中的有害成分去除,烟尘过滤装置流下的污水,则进入滤袋过滤装置8,由滤袋将脏物过滤;自滤袋8流出的水液则经水液处理装置101,渐次将水液中的细微杂质沉淀,使得处理后的水,可以再回收循环利用。 To sum soot filter device 2, the bag filter means 8, and the aqueous liquid processing apparatus 101, found dirty gas filtration system of the present invention, first filter means 2 to the dust or dirty gas in the high pressure gas hazardous component removing soot filter since aqueous effluent bag 8 is the liquid processing apparatus 101 by the water, the water was gradually fine precipitation of impurities, such processing; sewage flow means, the filter means 8 into the bag, the bag filter dirt water, can be recycled and re-used. 再者,对烟尘浓度高的污浊气体,可先经粒状烟尘收集装置3收集后,再送入烟尘过滤装置8中。 Furthermore, high concentrations of dust polluted gas can after collecting the particulate collection device 3 smoke, soot filter and then into the device 8. 以减轻烟尘过滤装置的负担。 Means to alleviate the burden of the soot filter. 对污浊程度轻的污水,可直接令其进入简便型滤袋污水处理装置8或再回收利用,以便缩短本过滤系统的过滤程序。 Mild degree of contamination of the water, directly into the make simple bag-type sewage treatment unit 8 or be recycled in order to shorten the filtration system of the present application.

Claims (29)

1.污浊气体过滤系统,有烟尘过滤装置,其特征在于:它由迂回式烟尘过滤装置2、滤袋过滤装置8、水液处理装置101,烟尘收集装置3组构而成,烟尘过滤装置本身是一迂回或螺旋盘绕式管道2,在管道2内设置有若干强力喷雾器组6,经烟尘过滤装置过滤后流下的污水经其自身底部设置的污水下流管道25流出并进入到滤袋过滤装置81过滤,然后流入具有复数个串连沉淀槽1014的水处理装置101中净化处理后再返流至烟尘过滤装置内的各强力喷雾器组6循环使用,经烟尘过滤装置2过滤后的新鲜烟气经其自身上部的烟气排出通道21排出,污浊气体是由烟尘过滤装置2底部的废气管1直接进入到迂回或螺旋盘绕式管道2中进行直接过滤或先进入烟尘收集装置3后、再进入到烟尘过滤装置2中进行过滤的,在烟尘过滤装置2内设置有强力送风机4。 1. dirty gas filtration system with smoke filter means, characterized in that: it is filtered by the dust circuitous apparatus 2, bag filter means 8, the liquid processing apparatus 101 water, dust collecting means 3 from fabric, dust filter means per se It is a circuitous or spiral wound conduit 2 disposed in the conduit 2 has several strong nebulizer group 6, downstream of the sewage pipe smoke through the filter apparatus through the bottom of the sewage flows down its own set of 25 and flows out into the bag filter means 81 filtered, and then flows into the flue gas with the fresh water treatment apparatus 101 after the plurality of series of precipitation tank 1014 and then reflux to the purification of smoke in each group in the nebulizer strong filtering 6 recycling means, the filtering device 2 by the soot filter after which the flue gas exhaust pipe itself an upper discharge passage 21 is discharged by the dirty gas is a soot filter apparatus directly into the bottom 2 to a bypass conduit or spiral wound filtration or 2 directly into the first dust-collecting device 3, and then proceeds to 2 soot filter apparatus for filtering, filter means disposed in the soot blower 2 with a strong 4.
2.按照权利要求1所述的污浊气体过滤系统,其特征在于:迂回式烟尘过滤装置2的主体为一S形的迂回管道2,强力喷雾器组6分别设置在S形迂回管道2的直立管段和横向管段的顶部,在S形迂回管道2的最上部有一烟气出口端21,S形迂回管道2的底部有一废气排入管1,强力送风机4设置在废气排入管1一侧,在S形迂回管道2的底部另一侧有一污水出口管25。 2. The system of claim dirty gas filter of claim 1, wherein: the soot filter body circuitous apparatus 2 is a S-shaped bypass pipe 2, a strong nebulizer group 6 are provided at the S-shaped pipe section upstanding bypass conduit 2 and a top transverse pipe section, the S-shaped bypass uppermost pipe 2 is provided with a flue gas outlet end 21, S-shaped bypass bottom of the pipe 2 has an exhaust gas into the pipe 1, a strong blower 4 is provided on a side of the exhaust gas into the tube, in the other side of the S-shaped bypass pipe 2 is provided with a bottom water outlet pipe 25.
3.按照权利要求2所述的污浊气体过滤系统,其特征在于:S形迂回管道2的底部的废气排入管1固定在与S形迂回管道2相连接的短管段24底部,短管段24有一环弧形的冷却水通入的冷却空间244,短管段24上外引连有与冷却空间244相贯通的冷却水进管241和冷却水出管245,S形迂回管道2由数个横向长管段和与横向长管段两头相连接的接头23连构而成。 3. The filter as claimed in claim dirty gas system of claim 2, wherein: S-pattern of the bypass exhaust pipe 2 into the bottom of the tube 1 is fixed to the bottom 2 and the S-shaped bypass pipe is connected to a short pipe section 24, a short pipe section 24 a cooling space part arcuate cooling water into the 244, a short pipe section 24 outer lead is connected with a cooling space 244 through the cooling water intake pipe 241 and a cooling water outlet pipe 245, S-shaped bypass pipe 2 by a plurality of transverse long pipe length and a transverse tube section connecting two joint configuration 23 connected together.
4.按照权利要求3所述的污浊气体过滤系统,其特征在于:冷却水进水管241有一圆弧形管部,与圆弧形管部的两下端分别水平延伸有一水平管部242,水平管部242上开设有复数的小出水口243。 4. The dirty gas filtration system of claim 3, wherein: a cooling water inlet pipe 241 has a circular arc-shaped tube section, and the two circular arc-shaped lower end portion of the tube extend horizontally with a horizontal portion 242, a horizontal tube portion 242 defines a plurality of small outlet 243.
5.按照权利要求2所述的污浊气体过滤系统,其特征在于:直立式强力喷雾器组602设置在各接头23内侧,各接头23分别与复数的各横向管段相吻合连接,各横向管段断面为圆管形或方形管或长方形管,强力喷雾器组603均设置在各横向管段顶部,在强力送风机4侧设置有强力喷雾器组601,各接头23呈长箱形,其外侧开有装放强力喷雾器组602的豁孔。 5. The claim dirty gas filtration system of claim 2, wherein: Upright strong nebulizer group 602 disposed in the joint 23 inside the joints 23 are respective transverse tube sections plurality coincide connection, each of the lateral pipe cross section is round pipe-shaped or square tubes or rectangular tubes, strength nebulizer group 603 are disposed at the top of each lateral pipe, there is strong nebulizer group 601 in a forced air blower 4 side, the joints 23 elongated box shape, which side opening has mounted put strong sprayer group excluded hole 602.
6.按照权利要求2或5所述的污浊气体过滤系统,其特征在于:各强力喷雾器组602和603分别与各接头23和各横长管段顶部的预留豁孔相扣放连接,在连接处周边配合垫放有防漏垫片,迂回管道2的下半部横向管段上装设的强力喷雾器组603的喷水方向与废气流动方向相同,迂回管道2的上半部横向管段上装设的强力喷雾器组603的喷水方向与废气流动方向相反,在烟气出口端21内有一滤水刷件22。 6. The system as claimed in claim 2 or dirty gas filter of claim 5, wherein: each of strong sprayers 602 and 603 respectively group the joints 23 and the top of each hole reservation excluded horizontally long interlocking discharge pipe connected, at the periphery of the connection leak-proof gasket with the pad placed, the same direction is mounted on the bypass water pipe lower half of the transverse tube section 2 nebulizer powerful set 603 with the exhaust gas flow direction, is mounted on the bypass pipe upper half of the transverse pipe section 2 nebulizer strong group water with the exhaust gas flow direction 603 opposite direction, the brush member 22 has a drainage outlet end 21 in the flue gas.
7.按照权利要求6所述的污浊气体过滤系统,其特征在于:各长箱形的接头23的外凸圆盘法兰与各横向管段2相连接,各强力喷雾器组602、603为长板形或圆盘形或弧板形的具有多组强力喷雾器组的板型座结构,各喷雾器组602、603周边设有凸缘231及与接头23和各横向管段2连接的螺栓孔,各长板形或圆盘形喷雾器组602、603的形状应与所装设的接头23和各横向管段外形形状相吻合。 7. A dirty gas filtration system of claim 6, wherein: each convex disc flange long box-shaped joint 23 to the transverse pipe section is connected to each of 2, 602, 603 of each group is a strong long plate nebulizers plate-shaped structure having a plurality of sets of strong base groups sprayer disk-shaped or arc-shaped or plate-shaped, each set of sprayers 602 is provided outside the bolt holes 231 and connected to the joint 23 and the flange of each lateral pipe 2, each of length shape of the plate or a disc atomizer group 602 should coincide with the lateral joint 23 and each of the outer shape of the pipe sections mounted.
8.按照权利要求6所述的污浊气体过滤系统,其特征在于:各强力喷雾器组602、603为安装在管件60上且具有不同喷射方向的单管形结构。 8. The system of claim dirty gas filter of claim 6, wherein: each of the groups 602, 603 mounted sprayers strength and having a single tubular structure different from the ejection direction to the tube member 60.
9.按照权利要求1所述的污浊气体过滤系统,其特征在于:螺旋盘绕式管道2为圆筒形或锥筒形,在筒腔内有一螺旋导板3,在螺旋导板3中央部位设有水液下流中管31,在水液下流中管31与螺旋导板接触部位开设有与水液下流中管31相贯通的复数下流孔洞32,在筒腔内壁处配置有强力喷雾器组6,在筒腔底部设置有与过滤装置相贯通的污水排出管25及废气排入管1。 9. The system of claim dirty gas filter of claim 1, wherein: a spiral wound conduit 2 as a cylindrical or tapered cylindrical, with a helical guide plate 3 in the cylinder cavity, with the central portion of the water in the coil guide plate 3 liquid downflow pipe 31, the pipe 31 and the spiral guide plate contact portion defines with aqueous downstream pipe 31 through a plurality of downstream apertures 32, disposed in the inner wall of the barrel chamber with a strong atomizer group 6 in the aqueous liquid downstream in the barrel chamber and filter means provided at the bottom with sewage through discharge pipe 25 and into the exhaust pipe 1.
10.按照权利要求9所述的污浊气体过滤系统,其特征在于:圆筒形的螺旋式盘绕管道2的筒腔顶部有一L形排烟管21,L形排烟管末端设有防尘盖211,在筒腔中部设置有一抽水泵5,水液下流中管31下部与连接管51连通,抽水泵5的水液泵送方向与废气流动方向相同,在筒腔下部设有人孔22,在废气排入管1一侧设有强力喷雾器61和强力送风机4。 10. The dirty gas filtration system of claim 9, wherein: the top of the chamber helically coiled tubular conduit 2 of a cylindrical shaped exhaust pipe has an L-21, L-shaped end of the exhaust pipe is provided with a dust cover 211, in the central cylindrical chamber with a water pump 5, aqueous liquid downflow pipe 31 the lower portion of the connection pipe 51 communicating, pumps same water pump feeding direction of the exhaust gas flow direction 5, is provided with a manhole at the cylinder lower chamber 22 is provided, in side exhaust pipe 1 into the sprayer 61 has a power and a power blower 4.
11.按照权利要求9所述的污浊气体过滤系统,其特征在于:下大上小的锥筒形螺旋式盘绕管道2的横截面形状均为圆形或椭圆形,筒腔顶部为一周高中低的倾斜顶板21,顶板21中央有一向下延伸的流通管211,流通管211对准下流中管31的孔口,在筒腔中部设置有一抽水泵5,水液下流中管31下部与连接管51连通,抽水泵5的水液泵送方向与废气流动方向相同,在筒腔下部设有人孔22,在筒腔底部的底板24上有复数根废气排入管1,在废气排入管1一侧设有强力喷雾器61和强力送风机4。 11. The dirty gas filtration system of claim 9, wherein: the large cross-sectional shape of a small cone cylindrical spiral wound pipe 2 are circular or elliptical, cylindrical chamber to the top of the low one week school the top plate 21 is inclined, the center of the top plate 21 has a downwardly extending flow pipe 211 and circulation tube 211 aligned with the aperture 31 of the downstream pipe is provided with a water pump 5, the lower portion of the connecting pipe 31 downstream pipe aqueous cartridge chamber in the middle communication 51, water feed pump pumps the same direction with the exhaust gas flow direction 5, a manhole 22 provided in the cylinder lower chamber, with a plurality of exhaust gas into the root canal at the bottom of the base plate 1 on the cylinder chamber 24, the exhaust gas discharged into the tube 1 side of the sprayer 61 has a power and a power blower 4.
12.按照权利要求2所述的污浊气体过滤系统,其特征在于:迂回式管道2为锯齿形管道,在锯齿形管道底部筒腔内底板24上部有一高压废气排入管1和废气排入管11,在锯齿形管道筒腔顶部有一清新气体排出管21,在锯齿形管道筒腔内壁上安装有强力喷雾器组601、602和603,在筒腔底部邻近底板24一侧内壁上倾斜设置有一挡板23,在挡板23上端与筒腔内壁之间有一强力弹簧22,底板24一侧有一污水排出管25。 12. The dirty gas filtration system of claim 2, wherein: the bypass conduit serrated pipe 2, a high pressure exhaust gas discharged into the exhaust pipe 1 and the pipe duct in an upper serrated cylindrical chamber bottom plate 24 11, there is a fresh gas exhaust pipe 21 at the top of the pipe barrel chamber zigzag, sawtooth-shaped cylindrical chamber wall of the pipe is fitted with strong nebulizer groups 601, 602 and 603, the bottom of the cylindrical chamber adjacent to the inner wall of the inclined base plate 24 side is provided with a stop plate 23, there is a strong spring 22 between the upper end 23 and the cylindrical cavity wall baffles, side plate 24 has a water discharge pipe 25.
13.按照权利要求12所述的污浊气体过滤系统,其特征在于:底板24呈倾斜状,挡板23上端与筒腔内壁固定并斜上延伸在高压废气排入管1管口上部,挡板23上端为自由端,各强力喷雾器组601、602和603相间隔装设在锯齿形管道2的各内壁侧,各强力喷雾器组601、602和603的喷射方向与废气流动方向相同,其中有一组强力喷雾器组603设置在锯齿形管道2的顶部水平壁面内壁处,其喷射方向与废气流动方向相反。 13. The dirty gas filtration system of claim 12, wherein: the base plate 24 is inclined, the shutter 23 fixed to the upper end of the cylindrical cavity wall and extending into the high pressure exhaust gas tube on the upper portion of a helical port shutter the upper end 23 is a free end, each of the groups 601, 602 and 603 strong sprayers mounted spaced apart in the inner wall of the pipe 2 is zigzag, the same as the ejection direction of exhaust gas flow direction 601, 602 and 603 in each group of strength sprayers, wherein a group of strong group sprayer 603 provided at the top horizontal wall surface of the inner wall of the sawtooth-shaped duct 2, which is the ejection direction opposite to the direction of flow of the exhaust gas.
14.按照权利要求12或13所述的污浊气体过滤系统,其特征在于:当锯齿形管道2底部筒腔的高压废气排入管1排出的废气压力达废气排放压力的85%时,压力控制开关将第一段强力喷雾器组601开启并开始喷射水雾当排出的废气压力达废气排放压力的90%时,压力控制开关第二段强力喷雾器组602开启并开始喷射水雾,当排出的废气压力达废气排放压力的95%时,压力控制开关将第三段强力喷雾器组603开启并开始喷射水雾,当废气排放压力达废气排放压力时,所有强力喷雾器组601、602和603同时开启。 14. The dirty gas filtration system of claim 12 or claim 13, wherein: when the high pressure exhaust gas conduit 2 at the bottom zigzag barrel chamber 1 into the exhaust pressure tube 85% of the exhaust gas discharged from the discharge pressure, the pressure control injection start switch is turned on and when the exhaust gas pressure water discharged from the exhaust emissions up to 90% of the pressure, the pressure control switch group 602 open second stage sprayer strong water sprays and start the first stage strong nebulizer group 601, when the exhaust gas discharged when the pressure reaches 95% of the exhaust gas discharge pressure, the pressure control switch is turned on and start the water sprays strong nebulizer third segment group 603, a pressure of exhaust emissions when the pressure of exhaust emissions, all strong sprayers 601, 602 and 603 simultaneously open group.
15.按照权利要求14所述的污浊气体过滤系统,其特征在于:当高压废气排入管1排出的废气排放压力逐渐回降至排放压力的85%以下时,压力控制开关将所有强力喷雾器组关闭并停止喷射水雾。 15. The dirty gas filtration system of claim 14, wherein: when the exhaust gas discharged from the discharge pressure of a high pressure exhaust gas discharged into the discharge tube gradually pressure was returned to 85% or less, the pressure control switch all groups strongly sprayers Close and stops the water sprays.
16.按照权利要求1所述的污浊气体过滤系统,其特征在于:烟尘过滤装置2为一横向直筒形,整个直筒形输气管分为201、202及203多段式结构,各输气段均设有气流调节式风扇52、53和54。 Claim 16. The dirty gas filtration system of claim 1, wherein: the soot filter device 2 is a straight transverse shape, straight shape entire pipeline 201, 202, and 203 into multi-stage configuration, each gas delivery sections are located fan has flow regulator 52, 53 and 54.
17.按照权利要求1所述的污浊气体过滤系统,其特征在于:烟尘过滤装置是由一下大上窄的梯形废气收集壳200及设置于废气收集壳200一侧的输气长管2以及输气长管2的中下部的与烟气冷却清洗器210之间的真空泵4构成,在梯形废气收集壳200顶部有一与输气长管2和废气收集壳200内腔相贯通的圆筒形烟尘集聚筒202,在废气收集壳两倾斜侧面设置有数个喷雾器装设口201,在各喷雾器装设口201处均设有喷雾器6,废气收集壳200底部有一污水收集槽203,输气长管2外侧设有数个内装有喷雾器6的喷雾器装设口28,真空泵4的排出管42与烟气冷却器210底部连通,真空泵4的吸入管41与输气长管2下部连通,输气长管2末端引连有与污水收集槽203相连通的污水排放支管205贯通的污水排放主管261,真空泵4由马达3驱转,废气收集壳200底壁的污水收集盘204上引通有与燃烧塔顶部相通 Claim 17. The dirty gas filtration system of claim 1, wherein: the soot filter 200 and the gas delivery apparatus 200 is disposed on the side of the exhaust-gas collection housing trapezoidal collected at the large shell on the narrow long tube 2 and an output gas in the lower portion of the long tube 2 of the scrubber the flue gas is cooled between 2104 pump configuration, there is a long tube with a cylindrical gas delivery dust collecting casing 2 and an exhaust phase through the lumen 200 at the top of the trapezoid-gas collection housing 200 agglomeration cylinder 202, the exhaust gas collecting housing two inclined side surfaces is provided with several sprayers mounting port 201, mounted in the mouth of the nebulizer 201 has a sprayer 6, the bottom of the gas collection housing 200 with a wastewater collection tank 203, gas pipe length 2 built with the outside provided with a plurality of sprayer sprayer 6 is mounted port 28, the bottom of the flue gas cooler 42 communicates with the discharge pipe 210 of the vacuum pump 4, the suction pipe of the vacuum pump 41 and gas transmission 4 2 lower communicating tube length, gas pipe length 2 terminal primer attached sewage discharge competent and sewerage groove 203 communicating sewage branch pipe 205 through 261, a vacuum pump 4 by the motor 3 driven forward, the leadthrough has the sewage collection pan 204 200 the bottom wall of the off-gas collection housing and the combustion column top communicate 排气口1,在排气口1周围设置有数个吹风管11,烟气冷却清洗器210为直式圆筒形,其上部有净气排出管212,其下部内壁环绕有冷却水管211,烟气冷却清洗器210底部与污水过滤槽8连通,污水过滤槽8一侧底部外引连有一与污水处理装置101或强力喷雾器6相引通的排水管89。 An exhaust port, an exhaust port is provided around several blowing pipes 11, cooled flue gas scrubber 210 is a straight cylindrical shape having an upper net gas discharge tube 212, which surrounds the lower portion of the inner wall of a cooling water pipe 211, smoke cooling air cleaner 210 communicates with the bottom of the filter water tank 8, the outer side of the water filtration tank bottom 8 has a lead connected to the sewage treatment apparatus 101 or power sprayer 6 with the drain pipe 89 through the lead.
18.按照权利要求17所述的污浊气体过滤系统,其特征在于:烟尘过滤装置的污水收集槽203下部有一底座601,烟冷却清洗器210的底部有一支承底座603,马达3下部有一支承底座602,废气收集壳200底部的污水收集盘204为倾斜状,在污水收集盘204的最低点有一与污水排放管支管205连通的污水收集口道206,冷却介质由冷却管进口2111引入并在螺旋冷却管211中循环后经出口2112离开烟气冷却清洗器210,在烟气冷却清洗器210内设置有防止水雾器溅的网件20,烟气冷却清洗器210底部与过滤槽8之间有一连通管213,过滤槽8内设置有过滤网206。 18. The claim dirty gas filtration system of claim 17, wherein: the soot sewage collecting tank lower portion 203 filtration apparatus has a base 601, a supporting base 603 bottom smoke cooling and cleaning 210, the motor 3 the lower part of a support base 602 sewage collection tray at the bottom of the gas collection case 200 204 is inclined, there is a sewage discharge pipe branch sewerage outlet channel communicating 205,206 at the lowest point of sewage collection pan 204, a cooling medium 2111 is introduced from the cooling pipe inlet and the coil cooling 20, a flue gas cooling and cleaning between the bottom of tank 210 and the filter 8 after the flue gas leaving the circulating cooling tube 211 via outlet 2,112,210 scrubber, mist with a mesh preventing member 210 is disposed in the splash-cooled flue gas scrubber communication pipe 213, the filter 8 is provided with a filter tank 206.
19.按照权利要求1或17所述的污浊气体过滤系统,其特征在于:烟尘过滤装置2的废气收集壳体200为长条形,在其底部污水收集盘204上间隔并列引入有三个燃烧塔的排气101、102和103,在各排气口周围均设置有吹风管组111、112和113,在废气收集壳体200一侧设置多个输气长管2、真空泵14及烟气冷却清洗器210和污水过滤槽8。 19. The dirty gas filtration system of claim 1 or claim 17, wherein: the soot filter housing gas collection device 200 is elongated, the introduction of three parallel combustion tower in the bottom plate 204 spaced sewerage 101, 102 and 103 of the exhaust gas, the exhaust ports are provided around each hair tube group 111, 112 and 113, a plurality of collector housing 200 side of the long tube 2 in the exhaust gas delivery, the vacuum pump 14 and cooled flue gas clean water filter 210 and the groove 8.
20.按照权利要求1所述的污浊气体过滤系统,其特征在于:烟尘过滤装置2为一横卧输气管,在输气管2内设置有喷雾器6和滤水网件20,在输气管2前端连接有网盖1,网盖1后部装设有吸尘装置41,在滤水网件20后部有刷式挡水器53,在输气管2出气端装有抽风扇4及驱动马达3,输气管2底部设有与轻便污水处理装置连通的污水排出管26,吸尘装置41及滤水网件20均由四根长杆形固定件7穿套连接。 Claim 20. The dirty gas filtration system of claim 1, wherein: the soot filter means 2 is a pipeline lying, is provided with a sprayer 6 and the net member 20 in the drainage pipeline 2, the front end of the pipeline 2 1 is connected with a mesh cover, a rear cover net mounted with the suction device 41, with a brush retaining member in the rear drainage network 2053, with the pipeline 2 downstream end of suction fan drive motor 3 and 4 , communicating with the portable water treatment apparatus sewage pipeline 2 at the bottom a discharge pipe 26, the suction device 41 and the water treatment network 20 by four pole-shaped fixing member 7 is connected through the sleeve.
21.按照权利要求20所述的污浊气体过滤系统,其特征在于:吸尘装置41为矩形框架,在矩形框架的支持架412上固定有数个风扇马达组411,吸尘装置41的四个直角端分别固定于四根长杆形固定件7的前段,各长杆形固定件7后段固定有多层网件20,各网件20外周有固定环201,各固定环201外圈固定在各长杆形固定件7上,各长杆形固定件7与输气管2内壁套合接触,挡水刷件53由固定环板51吊固,固定环板51外弧部设有把手52,固定环板51活动卡放在输气管2的锥形渐缩段起始处前的弧形缺口25内,喷雾器6分组设置在输气管2内周壁上并依等角间隔设置。 21. The filter as claimed in claim dirty gas system of claim 20, wherein: the suction device 41 in a rectangular frame, the rectangular frame holder 412 holds a plurality of groups of the fan motor 411, four right-angle suction device 41 ends are fixed to the pre-stage four pole-shaped fixing member 7, 7 after each segment has a long rod-shaped fixing element is fixed multilayer web member 20, the outer periphery 20 of each network element has a fixed ring 201, each of the fixing ring 201 is fixed to the outer ring each pole-shaped fixing member 7, each of the long rod-shaped fixing member 7 into contact with the pipeline inner wall nested, retaining the brush member 53 by a fixing ring 51 suspended solid plate, fixing plate ring 51 provided with a handle 52 outside the arc portion, the fixed plate 51 movable clamping ring on the pipeline 2 tapered cone 25, the sprayer 6 disposed spaced arcuate cutout packet before the beginning of the segment in the pipeline and the inner peripheral wall by an isometric 2.
22.按照权利要求1所述的污浊气体过滤系统,其特征在于:烟尘收集装置3的收集器部分为一烟尘收集筒,在烟尘收集筒两侧设有滴水收集槽33,烟尘收集筒的上半筒腹复盖有渗水网32,烟尘收集筒轴向一侧有一转轴34的传动装置7,转轴34穿过烟尘收集筒后由转轴支承架62支承,烟尘收集筒的左端面上开有冷气输送口35,收集筒右端为封闭状,烟尘收集筒的下底部密接有烟尘抽吸管4,烟尘抽吸管4末端连有烟尘抽吸泵41,烟尘抽吸泵41出口端连有一由复数层滤筒构成的透气且具有伸缩性的滤袋81,在烟尘收集筒内腔的转轴34上固设有若干烟尘附着板组36,在烟尘附着板组上均开设有长孔362,在长孔362内活动卡装有与烟尘附着板36两侧面贴附的滑条361,烟尘收集筒右侧筒腹中外引连有一烟气连管10,烟气连管10外延端与烟尘过滤装置2的废气排入管1连通,烟尘收 Claim 22. The dirty gas filtration system of claim 1, wherein: dust collector means for collecting portion 3 is a fume collection tube, is provided with grooves on both sides of the drip collecting tube 33 collecting dust, fume collection tube covered with a semi-cylindrical abdominal seepage network 32, fume collection tube axial side on a shaft 34 of the transmission 7, the rotating shaft 34 after passing through the dust collecting tube 62 is supported by the shaft supporting frame, a left end surface of the dust collection tube opening air-conditioned the delivery port 35, the collection tube is closed at the bottom right-shaped, cylindrical dust collecting adhesion with smoke suction tube 4, the suction tube 4 ends to smoke with smoke suction pump 41, the outlet end of the dust suction pump 41 is connected with a plurality of stretchable bag 81 and having a gas-permeable layer composed of cartridge, on the rotary shaft cylinder 34 fume collection chamber has a plurality of solid dust attachment plate group 36, dust adhered on the plate were set up a long hole 362, long with the bore 362 and the movable clamping plate 36 attached to both side surfaces of dust attached to the slider 361, the right cylindrical dust collection tube outer lead connected with a belly flue tube 10 is connected, even the flue gas pipe 10 and the end of the soot filter means epitaxial 2 1 into the exhaust pipe in communication, dust yield 筒一侧有一与烟尘过滤装置2的污水排出管25连通的污水容纳槽80,污水容纳槽80底部外连有数根供水支管803,供水支管803末端又连有一置于烟尘收集筒顶部的滴水横管802。 Tube side has a with dust filtering device sewage 2 discharge communication pipe 25 the sewage holding tank 80, an outer bottom water receiving groove 80 even several root water supply branch pipe 803, the water supply branch pipe 803 end in turn is connected with a disposed dripping horizontal top fume collection tube tube 802.
23.按照权利要求22所述的污浊气体过滤系统,其特征在于:烟尘收集筒一侧开有人孔31,烟尘抽吸管4由数个固定环42固定于烟尘收集筒底部轴向,沿烟尘收集筒顶部轴向设置的滴水横管802上开有若干个滴水孔,滴水孔滴下水液滴至收集筒上所复盖的渗水网32上,经渗水网32流下的水滴入水滴收集槽33内后被送至污水处理装置101或8中,各供水支管803并列设置呈摇把形并与污水容纳槽80和滴水横管802连通,污水容纳槽80上端外引连有污水溢流管801,污水溢流管801与水处理装置连通,转轴34一端与传动装置7驱连,其另一端支放在轴承座621内,轴承座621固定在梯形支持架62上,各冷气输送口35的开口大小可调节,位于烟尘收集筒筒腹段长上的转轴34的轴向间隔固套有数个附着板组36,在转轴34的轴向的附着板组36间隔处的转轴上固定有轴环371,轴环371的径向外伸有 23. The dirty gas filtration system of claim 22, wherein: one side open fume collection tube was holes 31, dust suction pipe 4 by a plurality of fixing rings 42 fixed to the bottom of the dust collecting cylinder axial direction dust drip collecting cylinder top cross tube 802 axially disposed opening with a plurality of drip holes, dripping water drops dripping hole on the cartridge to collect the seepage covered network 32, network 32 via a stream of water seepage droplets into the collection tank 33 drops after being supplied to the sewage treatment apparatus 101, or 8, each of the water supply branch pipe 803 are juxtaposed and shaped as a crank handle receiving slot 80 and with the waste water drip cross tube 802 communicates sewage holding tank 80 is connected an upper end of the outer lead sewage overflow pipe 801 sewage overflow pipe 801 communicates with the water treatment device, one end of the rotary shaft 34 and the drive gear 7 is connected, the other end 621 supported on the bearing seat, the bearing block 621 secured to the trapezoidal holder 62, each of the cool air delivery port 35 opening size can be adjusted, positioned axially on the cylinder barrel fume collection abdominal segment length of the shaft 34 spaced sets of several solid attachment plate group 36 in the axial direction of the rotary shaft 36 at intervals of the rotation shaft 34 is fixed to the attachment plate group collar 371, a radially extending collar 371 has an outer 距180度的径向杆37,各径向杆37的顶端固连有压缩弹簧372,各压缩弹簧372的另一端分别与二横向长刮条38内侧连接,横向长刮条38沿筒腹轴向分布并与筒腹内周壁接触,各烟尘附着板组36呈放射状沿转轴34径向分布,在各附着板组36的每块附着板的径向开有二对直立形长孔362,在直立形长孔362中活动卡套有与附着板组36等宽的横向滑条361,各横向滑条361与附着板组36两侧面接触滑动,在烟尘收集筒筒腔底部沿轴向间隔开设有落尘出口39,对应于各落尘出口39的相对应位置的烟尘抽吸管4上开有落尘吸入口43。 180 degrees from the radial rods 37, each of the radial rods 37 secured to the top compression spring 372, the other end of each of the compression springs 372 are connected to the two inner lateral length of the wiper strip 38, transverse strip 38 along the length of blade ventral axis cylindrical distribution and in contact with the cylindrical circumferential wall of the abdomen, each of the dust attachment plate 36 radially along the rotating shaft 34 set radially distributed, open upright long hole-shaped two pairs of attachment plate 362 in the radial direction in each attachment plate of each group 36, in vertical long hole 362 formed in the ferrule has the active plate set 36 attached to the transverse width of the slider 361, each of the slide bar 361 laterally in contact with the sliding plate 36 attached to both side surfaces of the group, at the bottom of the fume collection chamber axially spaced cylindrical barrel defines there dust outlet 39, corresponding to the position of each corresponding soot dust suction port 39 is opened in the suction port 43 on the dust suction pipe 4.
24.按照权利要求22所述的污浊气体过滤系统,其特征在于:滤袋过滤装置81是一具有内、中、外三层的具有不同网目的滤筒构成,内层滤筒813、中层滤筒812及外层滤筒811之间均有一环形空间,三层滤筒由连接带814及补强带815连固支承为一具有透气性且能伸缩的筒体81,其最内层滤筒孔目8131至最外层滤筒孔目8111的孔目逐渐变小。 24. The dirty gas filtration system of claim 22, wherein: a bag filter means 81 is an inner, middle and outer three-layer configuration having various mesh filter cartridge, the inner cartridge 813, the middle filter Each cartridge 812 between the cartridge 811 and an outer annular space, a three-layer tape cartridge 814 by the connecting and reinforcing tape 815 attached to a solid support capable of having air-permeable telescopic barrel 81, the cartridge innermost layer mesh mesh aperture hole 8131 to the outermost filter cartridge have openings 8111 becomes gradually smaller.
25.按照权利要求1或24所述的污浊气体过滤系统,其特征在于:滤袋过滤装置8上外引有与烟尘过滤装置2污水下流管道25引通的数根连管251,各污水连管251与一横向连管252连通,横向连管251与若干根竖直的L形短支管253连通,各L形短支管253下端均固套一长筒形滤袋81,各滤袋81的底端均坐放在长形大集水槽83内的支持网件82上部,各L形短支管253上设置有止水阀254,长形大集水槽83底部下连外探有数根与水液处理装置101相连通的下流管84。 25. The dirty gas filtration system of claim 1 or claim 24 wherein: a bag filter means 8 has an outer primer 2 and the soot filter means downstream of the sewage pipe 25 through a number of the primers with tube 251, and even various sewage tube 251 communicates with a transverse link tube 252, a transverse link tube 251 with a plurality of L-shaped vertical short root branch 253 communicates, each L-shaped lower end of the short branch pipes 253 are fixed sleeve 81 a long tubular filter bag, each bag 81 are seated in the bottom end of the support member web of large elongated upper portion 82 of the sump 83 is provided on each of the short L-shaped branch pipe 253 is connected with the outer probe several roots at the bottom of the water was large elongated sump 83 there is a valve seal 254, processing apparatus 101 through the downstream tube 84 is connected.
26.按照权利要求1所述的污浊气体过滤系统,其特征在于:水液处理装置101是一个具有若干个串连沉淀槽1012的长形槽体,在第一个沉淀槽1012前部串接有一内部装有搅拌器11的搅拌槽1011,最后一个沉淀槽1012的后部串接有一个内装有抽水管12、溢流管13和浮球阀90的清水槽1013,清水槽1013、搅拌槽1011及其间的各沉淀槽1012的上部均开设有流通孔1014,在各沉淀槽1012底部放置有污物附着板14,搅拌槽1011上部槽体内置放有滤袋装置8的下流管84,在清水槽1013上部有一清水辅助管9。 Claim 26. The dirty gas filtration system of claim 1, wherein: water is a liquid processing apparatus 101 form a plurality of elongated slot 1012 has a settling tank in series, 1012 series at a front portion of the first settling tank has an internal agitation tank equipped with a stirrer 11, 1011, the last precipitate a rear portion of the slot 1012 has a built in series with a suction pipe 12, clean water tank 13 and overflow pipe 90 of float valve 1013, 1013 clean-water tank, the stirring tank 1011 each settling tank between the upper portion 1012 and defines a passage hole are 1014, 1012 in the bottom of the settling tank is placed dirt adhering plate 14, the upper portion of the stirring tank 1011 with a bag placed within slot means 84 of the downstream pipe 8, Qing an upper auxiliary water tank 1013 has a pipe 9.
27.按照权利要求1或26所述的污浊气体过滤系统,其特征在于:水液处理装置101为圆槽形,各沉淀槽1012、搅拌槽1011及清水槽1013均为扇形槽体,各槽体上部均由流通孔1014互为串通,搅拌槽1011与清水槽1013之间不相通,搅拌槽1011上部放置有滤袋过滤装置8的下流管84。 27. The dirty gas filtration system of claim 1 or claim 26 wherein: aqueous liquid processing apparatus 101 is trough-shaped, each of the precipitation tank 1012 stirred tank clean-water tank 1011 and 1013 are groove segment thereof, each groove 1014 by the upper portion of the passage hole collusion each other, between 1011 and 1013 stirred tank clean-water tank not connected, upper stirring tank 1011 with a bag filter means disposed downstream of the tube 848.
28.按照权利要求1所述的污浊气体过滤系统,其特征在于:水液处理装置是由一封闭的箱体80,一置于箱体上部槽体内的滤袋81及箱体上部右侧的二高压喷雾机84及85构成,在箱体80下部的中部设有一多孔隔板83,多孔隔板83与多孔板861之间为一过滤夹层87,在多孔板861与座板853隔成的右下角箱体内探装有吸水管841和吸水管851,多孔隔板83左侧是一与置放有滤袋81的槽体相贯通的槽体。 28. The dirty gas filtration system of claim 1, wherein: the aqueous liquid processing means is a closed box 80, the upper portion of a housing groove disposed on the right side of the bag body 81 and the upper housing two high-pressure sprayers 84 and 85 constituted with a porous separator 83, a porous separator 83 between the perforated plate 861 and the interlayer 87 is a filter, the porous plate 861 and the base plate 853 in the central compartment 80 to the lower portion of the tank probe lower right corner cabinets with suction pipe 841 and suction tube 851, the left side of a porous separator 83 is placed with the tank body has a tank body of the bag 81 through the phase.
29.按照权利要求28所述的污浊气体过滤系统,其特征在于:水液处理装置8的箱体由隔板分隔成四个腔室,左上角腔室内放置有与烟尘过滤装置2的污水下流管25相连接的滤袋81,滤袋81下部的集水板82上开有一与其下腔室相通的集水口821,集水板82下部的腔室与其右侧下部装有浮球控制阀90的腔室相贯通,左、右两腔室间设有过滤夹层87,装有滤袋81腔室的右侧腔室内呈上下设置有二台高压喷雾机,二高压喷雾机84和85分别由座板843与853支持固定,二高压喷雾机84和85上外引连有出水管842和852,在右下方腔室内设有供水管9,箱体80前侧铰连有箱门801,箱门801上设有把手802。 Claim 29. The dirty gas filtration system of claim 28, wherein: the tank water liquid processing apparatus 8 is partitioned by a separator into four chambers, upper left corner of the chamber disposed downstream of the filter and the dust sewage apparatus 2 25 is connected to the bag 81 and its lower opening has a water collecting port communicating chamber 821 on the lower portion 82 of the bag 81 water-collecting plates, a lower water collecting plate 82 and its lower right portion of the chamber with float valve 90 phase through the chamber, between the left and right chambers is provided with a laminated filter 87, goes to the right side of the lower chamber is provided with the bag chamber 81 has two high-pressure sprayers, two high-pressure sprayers 84 and 85 respectively, by support plate 843 with the seat 853 is fixed, the two high-pressure sprayers 84 and 85 have outer leads attached outlet pipe 842 and 852, in the lower right chamber 9 is provided with a water supply pipe, the casing 80 has a hinged front door 801, box provided with a handle 802 on the door 801.
CN 92103597 1992-05-19 1992-05-19 Filtering system for muddy gas CN1070587A (en)

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US07/943,389 US5298043A (en) 1992-05-19 1992-09-10 Filter system for smoke or polluted air
AU43767/93A AU4376793A (en) 1992-05-19 1993-05-17 Filter system for smoke or polluted air
EP93913907A EP0641242A4 (en) 1992-05-19 1993-05-17 Filter system for smoke or polluted air.
CA 2136221 CA2136221A1 (en) 1992-05-19 1993-05-17 Filter system for smoke or polluted air
PCT/US1993/004622 WO1993023145A1 (en) 1992-05-19 1993-05-17 Filter system for smoke or polluted air
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AU4376793A (en) 1993-12-13
BR9306400A (en) 1998-09-15

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